TW574491B - Heat pump hot water supply device - Google Patents

Heat pump hot water supply device Download PDF

Info

Publication number
TW574491B
TW574491B TW92102791A TW92102791A TW574491B TW 574491 B TW574491 B TW 574491B TW 92102791 A TW92102791 A TW 92102791A TW 92102791 A TW92102791 A TW 92102791A TW 574491 B TW574491 B TW 574491B
Authority
TW
Taiwan
Prior art keywords
water supply
hot water
heat
temperature
flow path
Prior art date
Application number
TW92102791A
Other languages
Chinese (zh)
Other versions
TW200303407A (en
Inventor
Keijiro Kunimoto
Takeshi Watanabe
Ryuta Kondo
Satoshi Matsumoto
Satoshi Imabayashi
Original Assignee
Matsushita Electric Ind Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP2002033648A external-priority patent/JP3743375B2/en
Priority claimed from JP2002033650A external-priority patent/JP3815341B2/en
Priority claimed from JP2002041048A external-priority patent/JP3778102B2/en
Application filed by Matsushita Electric Ind Co Ltd filed Critical Matsushita Electric Ind Co Ltd
Publication of TW200303407A publication Critical patent/TW200303407A/en
Application granted granted Critical
Publication of TW574491B publication Critical patent/TW574491B/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00Details
    • F24D19/10Arrangement or mounting of control or safety devices
    • F24D19/1006Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1051Arrangement or mounting of control or safety devices for water heating systems for domestic hot water
    • F24D19/1054Arrangement or mounting of control or safety devices for water heating systems for domestic hot water the system uses a heat pump
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B30/00Heat pumps
    • F25B30/02Heat pumps of the compression type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D17/00Domestic hot-water supply systems
    • F24D17/02Domestic hot-water supply systems using heat pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/10Control of fluid heaters characterised by the purpose of the control
    • F24H15/174Supplying heated water with desired temperature or desired range of temperature
    • F24H15/175Supplying heated water with desired temperature or desired range of temperature where the difference between the measured temperature and a set temperature is kept under a predetermined value
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/212Temperature of the water
    • F24H15/215Temperature of the water before heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/212Temperature of the water
    • F24H15/219Temperature of the water after heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/212Temperature of the water
    • F24H15/223Temperature of the water in the water storage tank
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/238Flow rate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/258Outdoor temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/20Control of fluid heaters characterised by control inputs
    • F24H15/281Input from user
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/30Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
    • F24H15/375Control of heat pumps
    • F24H15/38Control of compressors of heat pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/30Control of fluid heaters characterised by control outputs; characterised by the components to be controlled
    • F24H15/375Control of heat pumps
    • F24H15/385Control of expansion valves of heat pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H15/00Control of fluid heaters
    • F24H15/40Control of fluid heaters characterised by the type of controllers
    • F24H15/414Control of fluid heaters characterised by the type of controllers using electronic processing, e.g. computer-based
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/06Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F25B2309/061Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/06Several compression cycles arranged in parallel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/07Details of compressors or related parts
    • F25B2400/075Details of compressors or related parts with parallel compressors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/02Compressor control
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/02Compressor control
    • F25B2600/021Inverters therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/02Compressor control
    • F25B2600/025Compressor control by controlling speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/11Fan speed control
    • F25B2600/112Fan speed control of evaporator fans
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2106Temperatures of fresh outdoor air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2116Temperatures of a condenser
    • F25B2700/21161Temperatures of a condenser of the fluid heated by the condenser
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Fluid Mechanics (AREA)
  • Computer Hardware Design (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Steam Or Hot-Water Central Heating Systems (AREA)

Description

574491 、、 、、'、'、Γ ”、、、、、' 、、…、、、、'、Ή' , 、、、、、、J 、、、、、、、、、一 s 、 、、、 、 、、、、、:: 、 、 、、 、、 、、 f 、、、、、'、、、、、:: : 7、::、、 【發明所屬之技術領域3 技術領域 本發明係有關於一種瞬間沸水型熱泵式熱水供應裝置 〇 5 【^SL 】 背景技術 迄今係使用利用燃燒瓦斯或石油之熱水供應機作為瞬 間沸水型熱水供應裝置。該等瞬間沸水型熱水供應裝置具 有溫度升高快,且展現出強大能力之特徵,相反地,亦有 10 因排氣而產生之空氣污染或對被直接燃燒的不安全感、燃 燒噪音等無法避免的問題。相對於此,將熱水儲存於大型 熱水儲存槽並供應熱水之熱泵式熱水供應器解決藉燃燒來 運作之熱水供應機的問題,而且因熱泵而具有較佳之熱效 率。但,前述熱水供應器有熱水儲存槽大、重量與設置空 15 間等施工上的問題。雖然有藉由用以解決大型熱水儲存槽 的問題之熱泵來達成瞬間沸水的想法,但熱泵的情形與燃 燒熱水供應機不同,熱泵循環機構之熱的升高需要時間。 因此,在熱水流出方面很花時間而令使用者感到不滿。又 ,熱泵係依氣溫或濕度或水溫等自然條件的不同來變化熱 20 水供應能力。而且,在熱水供應流量有變化之條件下要涵 蓋廣泛的熱水供應能力且維持快速而穩定的熱水供應溫度 是困難的。如此一來熱栗型熱水供應器在穩定地供應熱水 這一點上有困難。 於曰本專利公開公報特開平第2— 223767號係提出用 574491574491 ,,,,,,,,, Γ ,,,,,,,,, ... ,,,,,,,,,,,,,,,,, J ,,,,,,,,,,,,,,,,,,,,,,,,,, ,,,,,,,,::,,,,,,,,, F,,,,,, ',,,,::: 7, 7,: ,, [Technical Field to which the Invention belongs 3 Technical Field The present invention relates to Related to an instantaneous boiling water type heat pump hot water supply device 05 [^ SL] Background Art So far, a hot water supply device using combustion gas or petroleum has been used as an instantaneous boiling water type hot water supply device. Such instantaneous boiling water type hot water supply devices The device has the characteristics of rapid temperature rise and exhibits powerful capabilities. Conversely, there are also unavoidable problems such as air pollution caused by exhaust gas, insecurity to direct combustion, and combustion noise. In contrast, The heat pump type hot water supplier that stores hot water in a large hot water storage tank and supplies hot water solves the problem of hot water supply machines that operate by combustion, and has better thermal efficiency due to the heat pump. However, the aforementioned hot water supply The device has a large and heavy water storage tank. There are construction problems such as the installation of 15 spaces. Although there is an idea to achieve instant boiling water by using a heat pump to solve the problem of large hot water storage tanks, the situation of a heat pump is different from a combustion hot water supply machine. It takes time to increase the heat. Therefore, it takes time for hot water to flow out and makes users dissatisfied. In addition, the heat pump changes the heat supply capacity according to natural conditions such as air temperature or humidity or water temperature. It is difficult to cover a wide range of hot water supply capacity and maintain a fast and stable hot water supply temperature under conditions of changing hot water supply flow rates. In this way, the hot chestnut-type hot water supply device can stably supply hot water. There is a problem in the above-mentioned Japanese Patent Laid-Open Publication No. 2-223767.

玖、發明說明 以解決上述問題之瞬間沸水型熱泵式熱水供應裝置,其概 略構造顯示於第11圖。該熱泵式熱水供應裝置係包含有藉 冷媒流路201將壓縮機202、放熱器203、減壓部204、吸 熱器205連接成閉路之熱泵循環機構207。該熱泵式熱水 5 供應裝置更包含有:具有用以與前述放熱器203之冷媒流 路208進行熱交換之水流路209之熱交換器210、用以將 自來水供給至該水流路209之給水管211及用以連接該水 流路209與蓮蓬頭或水龍頭等熱水供應末端212之熱水供 應迴路213。再者,具有設在該熱水供應迴路213且用以 10 檢測熱水供應溫度之溫度感應器214及用以控制前述壓縮 機202的轉數之變換器215。而且,依照該溫度感應器214 之檢測溫度與設定溫度之差來變換輸出至壓縮機202之頻 率。即,於習知之熱水供應裝置中係控制成當熱水供應溫 度較設定溫度低時則增加該壓縮機202之轉數,而當熱水 15 供應溫度較高時則減少轉數。 於前述瞬間沸水型中熱水供應時之熱水供應負荷並不 一定,特別是由於使用者因熱水供應目的的不同而使流量 千變萬化,故熱水供應負荷會大幅改變。例如家庭用熱水 供應的情況,在供應熱水至對淋浴或泡澡裝滿熱水時為 20 10L/min至20L/min之大流量,而對在廚房清洗餐具或洗 臉供應熱水時則為3L/min至5L/min之小流量。又,熱水 供應負荷亦由於因季節不同而產生之給水溫度的變化而大 幅改變。 如此一來因流量或水溫的變化,熱水供應負荷會大幅 574491 、、發明說明 Μ—发明 Description of the invention The instantaneous boiling water heat pump type hot water supply device to solve the above problems is shown in Fig. 11 in outline. The heat pump hot water supply device includes a heat pump circulation mechanism 207 that connects a compressor 202, a radiator 203, a pressure reducing unit 204, and a heat sink 205 to a closed circuit through a refrigerant flow path 201. The heat pump type hot water supply device 5 further includes a heat exchanger 210 having a water flow path 209 for heat exchange with the refrigerant flow path 208 of the radiator 203, and a water supply for supplying tap water to the water flow path 209. A pipe 211 and a hot water supply circuit 213 for connecting the water flow path 209 to a hot water supply terminal 212 such as a shower head or a faucet. Furthermore, a temperature sensor 214 is provided in the hot water supply circuit 213 to detect the hot water supply temperature, and a converter 215 is provided to control the number of revolutions of the compressor 202. In addition, the frequency output to the compressor 202 is converted in accordance with the difference between the detected temperature and the set temperature of the temperature sensor 214. That is, in the conventional hot water supply device, it is controlled to increase the number of revolutions of the compressor 202 when the hot water supply temperature is lower than the set temperature, and to decrease the number of revolutions when the hot water supply temperature is higher. The load of hot water supply during the above-mentioned instantaneous boiling-type hot water supply is not constant, especially since the flow rate of the user varies greatly depending on the purpose of hot water supply, so the load of hot water supply will change significantly. For example, in the case of domestic hot water supply, when the hot water is supplied until the shower or bath is filled with hot water, the flow rate is 20 10L / min to 20L / min, and when the kitchen is washing dishes or washing the face, hot water is supplied. Small flow rate from 3L / min to 5L / min. In addition, the hot water supply load also changes greatly due to the change in the temperature of the feed water due to the different seasons. In this way, due to changes in the flow rate or water temperature, the hot water supply load will greatly increase 574491.

改變。相對於此,如習知之熱泵式熱水供應裝置僅以熱水 供應溫度與設定溫度之差來改變壓縮機之轉數且控制熱水 供應熱量時在控制之反應性與穩定性會產生不理想的情形 。例如,若降低熱水供應溫度與設定溫度之溫度差及壓縮 5 機之轉數間的係數,即控制增益以使控制之穩定性良好, 則轉數的變化量相對於溫度差的變化量會減少。因此,熱 水供應溫度變化會變緩慢,而到達設定溫度很花時間,且 因偏差而有不同的流量或水溫,因此熱水供應溫度之穩定 值不會達到設定溫度且會變化。若提高控制增益則在熱水 10 供應負荷大之大流量中,由於熱水供應溫度的變化相對於 壓縮機之轉數的變化少故可穩定地控制。但,在小流量之 熱水供應中,熱水供應溫度的變化相對於壓縮機之轉數的 變化會變得急遽。因此,不但壓縮機之轉數控制的變化變 得急遽且熱水供應溫度不穩定,也可能因相位的偏差引起 15 追逐現象而分散熱水供應溫度與轉數變化之控制。 又,瞬間沸水型熱泵式熱水供應裝置於開始供應熱水 時在升高熱泵循環機構整體的壓力或溫度時需要時間。因 此,相較於瓦斯熱水供應機等,從熱交換器之水流路供應 熱水會較慢。習知之構造中,在開始供應熱水時,係僅以 20 熱水供應溫度與設定溫度之差來設定壓縮機之轉數。因此 ,無論大流量或小流量皆如開始供應熱水時在熱水供應溫 度低之狀態下,壓縮機之轉數會同樣地設定為高標準。如 此一來,小流量時來自熱交換器之熱水供應溫度會急遽上 升且過衝。藉此有較設定溫度高溫之熱水流出,且因放熱 574491 ί 、 、 、 、 = S ' -SS 、V\ '、*·、、、、' 、 、 f 玖、'發明說明. _隱纖__議__鑰纖議_黎議謹鐘^ 器溫度的上升使壓縮機出口之壓力異常地變大等不理想的 情況發生。 再者,於習知之熱泵式熱水供應裝置中,雖然必須改 變單一的壓縮機202之運轉狀態,且改變轉數,但在僅改 5 變單一的壓縮機之轉數的控制中能力變更幅度有限。例如 無法涵蓋從冬天淋浴與泡澡時同時裝滿熱水之強大能力至 夏天的洗碗等微小能力之廣泛的熱水供應能力。因此會引 起淋浴溫度下降,而清洗餐具時流出熱水等不理想之情況 〇 10 又,若因氣溫或水溫或熱水供應負荷而改變熱泵循環 機構之運轉條件,則運轉效率亦有所變化。由於在習知之 熱泵式熱水供應裝置中僅依照熱水供應溫度來改變壓縮機 之轉數,故運轉效率會變化,且即使是加熱效率不良之條 件亦可繼續運轉。因此,因條件的不同,不僅是效率會極 15 端地惡化且能力會無法發揮,運轉成本亦會提高。 另一方面,為了縮短熱水開始供應時之流出熱水溫度 上升所需的時間,亦有設置與放熱器熱交換之熱水儲存槽 ,且以該熱水儲存槽包圍壓縮機之方法。於該構造中,由 於一旦供應熱水則將熱水儲存於熱水儲存槽,且即使提止 20 供應熱水,壓縮器亦不變冷,故再次供應熱水時可很快使 熱水供應溫度升高。 然而,一旦熱水儲存槽變冷則壓縮機亦會變冷,且會 反過來因被熱水儲存槽奪去壓縮機的熱而使熱泵循環機構 之溫度升高變慢。又,由於熱水供應係從熱水儲存槽進行 574491change. In contrast, the conventional heat pump type hot water supply device only uses the difference between the hot water supply temperature and the set temperature to change the number of revolutions of the compressor, and the control reaction and stability of the hot water supply heat are not ideal. Situation. For example, if the temperature difference between the hot water supply temperature and the set temperature and the number of revolutions of the compressor are reduced, that is, the gain is controlled to make the control stable, the amount of change in the number of revolutions relative to the temperature difference will be changed. cut back. Therefore, the hot water supply temperature changes slowly, and it takes time to reach the set temperature, and there is a different flow or water temperature due to the deviation, so the stable value of the hot water supply temperature will not reach the set temperature and will change. If the control gain is increased, it is possible to perform stable control in a large flow with a large supply load of hot water, since the change in the hot water supply temperature is less than the change in the number of revolutions of the compressor. However, in the hot water supply with a small flow rate, the change in the temperature of the hot water supply relative to the change in the number of revolutions of the compressor becomes sharp. Therefore, not only the change in the speed control of the compressor becomes drastic and the hot water supply temperature is unstable, but also the chase phenomenon caused by the phase deviation may disperse the control of the change in the hot water supply temperature and speed. In addition, the instant boiling water heat pump type hot water supply device requires time to increase the pressure or temperature of the entire heat pump circulation mechanism when hot water supply is started. Therefore, hot water supply from the water flow path of the heat exchanger is slower than that of a gas hot water supply machine. In the conventional structure, when the hot water supply is started, only the difference between the hot water supply temperature and the set temperature is used to set the number of revolutions of the compressor. Therefore, regardless of the large or small flow rate, when the hot water supply temperature is low at the beginning of hot water supply, the compressor's revolutions will be set to the same high standard. As a result, the hot water supply temperature from the heat exchanger will rise sharply and overshoot at low flow rates. As a result, hot water with a higher temperature than the set temperature flows out, and due to the exotherm 574491 ί,,,, = S '-SS, V \', * · ,,,, ',, f 玖,' Invention. _Crypto fiber __ 议 __Key Fibers _ Li Yiqin Zhong ^ The rise in the temperature of the compressor makes the pressure at the outlet of the compressor abnormally large, and other undesirable situations occur. Furthermore, in the conventional heat pump hot water supply device, although it is necessary to change the operating state of a single compressor 202 and the number of revolutions, the capacity change range is controlled by only changing the number of revolutions of a single compressor. limited. For example, it cannot cover a wide range of hot water supply capabilities, ranging from the powerful ability of filling hot water at the same time in the winter to showers and baths to the small capacity of washing dishes in the summer. As a result, the temperature of the shower will drop, and hot water may not flow out when washing dishes. 10 Also, if the operating conditions of the heat pump circulation mechanism are changed due to air temperature, water temperature, or hot water supply load, the operating efficiency will also change. . In the conventional heat pump type hot water supply device, the rotation speed of the compressor is changed according to only the hot water supply temperature, so the operation efficiency changes, and the operation can be continued even under the condition of poor heating efficiency. Therefore, due to different conditions, not only the efficiency will be extremely deteriorated and the capacity will not be exerted, but the operating cost will also be increased. On the other hand, in order to shorten the time required for the temperature of the outgoing hot water to rise when hot water starts to be supplied, there is also a method of setting a hot water storage tank for heat exchange with the radiator and surrounding the compressor with the hot water storage tank. In this structure, since the hot water is stored in the hot water storage tank once it is supplied, and the compressor does not cool even if the hot water supply is stopped at 20, the hot water supply can be made quickly when the hot water is supplied again The temperature rises. However, once the hot water storage tank becomes cold, the compressor also becomes cold, and the temperature of the heat pump circulation mechanism becomes slower because the heat of the compressor is taken away by the hot water storage tank. In addition, since hot water supply is performed from a hot water storage tank, 574491

οοΒίχαο明說明οοΒίχαο Description

,故一旦該熱水儲存槽之溫度變冷,則流出熱水溫度亦變 冷,且至熱水儲存槽之熱水溫度上升為止,流出熱水溫度 不會上升。因此,來自熱水儲存槽變冷之狀態的熱水供應 至熱水流出為止反而需要更多時間。 5 如上所述,於習知之熱泵式熱水供應裝置中,由於與Therefore, once the temperature of the hot water storage tank becomes cold, the temperature of the outflow hot water also becomes cold, and the temperature of the outflow hot water does not increase until the temperature of the hot water in the hot water storage tank rises. Therefore, it takes more time for the hot water supply from the state in which the hot water storage tank is cooled until the hot water flows out. 5 As mentioned above, in the conventional heat pump hot water supply device,

熱水供應負荷大小無關一律進行加熱控制,故不易應付廣 泛的熱水供應負荷。又,不易使熱水溫度控制之反應性與 穩定性並存。而且,有時反倒使熱水供應溫度之升高變差 ,且有降低效率等問題。 10 【發明内容】 發明之揭示The hot water supply load is controlled regardless of the size of the hot water supply load, so it is not easy to cope with a wide range of hot water supply loads. In addition, it is difficult to coexist the reactivity and stability of hot water temperature control. In addition, it sometimes worsens the increase in hot water supply temperature and reduces efficiency and other problems. 10 [Summary of the Invention] Disclosure of the Invention

本發明之熱水供應裝置係包含有:熱泵循環機構,具 有:壓縮機、放熱器、減壓部、吸熱器及使前述壓縮機、 前述放熱器、前述減壓部及前述吸熱器構成為閉路之冷媒 15 流路;熱交換器,具有用以與前述冷媒流路進行熱交換之 水流路;給水管,用以將自來水供給至前述水流路;及熱 水供應迴路,係連接成可從前述水流路通水至熱水供應末 端者。該熱水供應裝置更包括: 1) 用以設定於前述熱交換器之加熱量之負荷設定部及 20 依照該設定值來控制加熱量之加熱控制部; 2) 用以加熱含有前述熱交換器之水流路之前後通路的 水之加溫部; 3) 多數壓縮機;及 4) 多數熱泵循環機構 10 574491 玖、,發明說明 、、·Ν ·Χ、\、、 :V、' 'V、、: >、 、' ί ::。人 S …:、::'、ΛΛ:'、、,、、、、:、、、 ::、… 、 '、:: …Ά、:、'、- ΐ' 之其中一者。 圖式簡單說明 第1圖係本發明第1實施形態之熱泵式熱水供應裝置 的構成圖。 5 第2圖係本發明第2實施形態之熱泵式熱水供應裝置 的構成圖。 第3圖係本發明第3實施形態之熱泵式熱水供應裝置 的構成圖。 第4圖係本發明第4實施形態之熱泵式熱水供應裝置 10 的構成圖。 第5圖係本發明第5實施形態之熱泵式熱水供應裝置 的構成圖。 第6圖係本發明第6實施形態之熱泵式熱水供應裝置 的構成圖。 15 第7圖係本發明第7實施形態之熱泵式熱水供應裝置 的構成圖。 第8圖係本發明第8實施形態之熱泵式熱水供應裝置 的構成圖。 第9圖係本發明第9實施形態之熱泵式熱水供應裝置 20 的構成圖。 第10圖係本發明第10實施形態之熱泵式熱水供應裝 置的構成圖。 第11圖係習知之熱泵式熱水供應裝置的構成圖。 11 574491 德耀冀数飄麵S纖錄择纖,燃燃烫凝願緣纖攤驗麵::顆:$释:s恶: 工/r 口口^^口口 疚〜發明說明 驗鐵纖縫纔纖齡錄纖纖鑛鐵_應纖鑛^§«^纖5;怨麵纖纖纖鐵鑛嫌鑛纖纖鑛錄_錄纖魏凝湯鑛成纖 實施發明之最佳形態 以下就本發明之實施形態,一面參照圖示一面說明。 且,於各實施形態中,就相同構造、作相同動作的部分則 賦予同一符號,且省略詳細之說明。 5 (第1實施形態)The hot water supply device of the present invention includes a heat pump circulation mechanism including a compressor, a radiator, a decompression unit, a heat sink, and a closed circuit configured by the compressor, the heat sink, the decompression unit, and the heat sink. 15 refrigerant flow paths; a heat exchanger having a water flow path for heat exchange with the refrigerant flow path; a water supply pipe for supplying tap water to the water flow path; and a hot water supply circuit connected to be connected from the foregoing Water flows to the end of the hot water supply. The hot water supply device further includes: 1) a load setting section for setting the heating amount of the heat exchanger and a heating control section for controlling the heating amount according to the set value; 2) a heating device containing the foregoing heat exchanger The water heating part of the water path before and after the water flow path; 3) most compressors; and 4) most heat pump circulation mechanisms 10 574491 ,, description of the invention, ···· ×, \ ,,: V, '' V, ,: ≫,, ί ::. Person S…:, :: ', ΛΛ:' ,,,,,,,: ,,, :::, ..., ', :: ... Ά,:,',-ΐ '. Brief Description of Drawings Fig. 1 is a block diagram of a heat pump type hot water supply device according to a first embodiment of the present invention. 5 FIG. 2 is a configuration diagram of a heat pump type hot water supply device according to a second embodiment of the present invention. Fig. 3 is a configuration diagram of a heat pump type hot water supply device according to a third embodiment of the present invention. Fig. 4 is a configuration diagram of a heat pump hot water supply device 10 according to a fourth embodiment of the present invention. Fig. 5 is a configuration diagram of a heat pump type hot water supply device according to a fifth embodiment of the present invention. Fig. 6 is a configuration diagram of a heat pump type hot water supply device according to a sixth embodiment of the present invention. 15 FIG. 7 is a configuration diagram of a heat pump type hot water supply device according to a seventh embodiment of the present invention. Fig. 8 is a configuration diagram of a heat pump type hot water supply device according to an eighth embodiment of the present invention. Fig. 9 is a configuration diagram of a heat pump hot water supply device 20 according to a ninth embodiment of the present invention. Fig. 10 is a configuration diagram of a heat pump type hot water supply device according to a tenth embodiment of the present invention. Fig. 11 is a block diagram of a conventional heat pump hot water supply device. 11 574491 Deyao Ji number floating surface S fiber recording fiber selection, burning and burning condensed edge fiber booth inspection surface :: piece: $ 释: s evil: 工 / r 口 口 ^^ 口 口 口Secret fiber age record fiber fiber ore iron _ should fiber ore ^ § «^ fiber 5; complaint surface fiber fiber fiber iron ore suspected fiber fiber ore record _ record fiber Wei Ning Tang ore fiber forming the best form of the invention The following is the embodiment of the present invention , While referring to the illustration. In addition, in each embodiment, parts having the same structure and the same operation are given the same symbols, and detailed descriptions are omitted. 5 (first embodiment)

第1圖係本發明第1實施形態之熱泵式熱水供應裝置 的構成圖。第1圖中,於熱泵循環機構7中係藉由冷媒流 路1將壓縮機2、第1放熱器3Α、第2放熱器3、減壓部 4及吸熱器5連接成閉路。熱泵循環機構7為使用例如二 10 氧化碳作為冷媒,且高壓側之冷媒壓力在冷媒之臨界壓力 以上之超臨界熱泵循環機構。壓縮機2係藉由内藏之電動 馬達(未圖示)來驅動,且使所吸引之冷媒壓縮至臨界壓力 並排出之。又,熱交換器10係具有用以與第2放熱器3之 冷媒流路8進行熱交換之水流路9。用以將自來水直接供 15 給至水流路9之給水管11係與可使從水流路9流出之熱水 通水至由蓮蓬頭16或水龍頭17等所構成之熱水供應末端 12之熱水供應迴路13相連接。而且,用以加熱熱水供應 迴路13的水之加溫部38係由並列地連接於熱水供應迴路 上游部39之蓄熱部40所構成。蓄熱部40係由用以儲存熱 20 水供應迴路13的流水之儲存槽41及用以混合上游部39與 蓄熱部40的流水之混合閥34所構成。儲存槽41係構造成 下端為入口管43,而上端為出口管44,且下部内藏有第1 放熱器3Α,並以隔熱材料45覆蓋者。第1放熱器3Α係 兼具用以將儲存槽41内之蓄熱溫度(以下,稱作儲存溫度) 12 574491Fig. 1 is a configuration diagram of a heat pump type hot water supply device according to a first embodiment of the present invention. In Fig. 1, in the heat pump circulation mechanism 7, the compressor 2, the first radiator 3A, the second radiator 3, the pressure reducing unit 4, and the heat absorber 5 are connected in a closed circuit through a refrigerant flow path 1. The heat pump cycle mechanism 7 is a supercritical heat pump cycle mechanism using, for example, carbon dioxide as the refrigerant, and the pressure of the high-pressure side refrigerant is above the critical pressure of the refrigerant. The compressor 2 is driven by a built-in electric motor (not shown), and the sucked refrigerant is compressed to a critical pressure and discharged. The heat exchanger 10 has a water flow path 9 for exchanging heat with the refrigerant flow path 8 of the second radiator 3. The water supply pipe 11 for directly supplying the tap water 15 to the water flow path 9 is a hot water supply that allows hot water flowing from the water flow path 9 to pass through to the hot water supply end 12 composed of a shower head 16 or a water tap 17 The circuits 13 are connected. The heating section 38 for heating the water in the hot water supply circuit 13 is constituted by a heat storage section 40 connected in parallel to the hot water supply circuit upstream section 39. The heat storage section 40 is composed of a storage tank 41 for storing the flowing water of the water supply circuit 13 and a mixing valve 34 for mixing the flowing water of the upstream section 39 and the heat storage section 40. The storage tank 41 is configured such that the lower end is an inlet pipe 43 and the upper end is an outlet pipe 44, and a first radiator 3A is built in the lower part and covered with a heat insulating material 45. The first heat radiator 3A series also has a temperature for storing heat in the storage tank 41 (hereinafter, referred to as storage temperature) 12 574491

玖、發明說明 毅毅漏§纖§毅纖纖凝駿:»»纖驗 保持於預定溫度之保溫部。熱水供應迴路13係從分歧部 46分歧為上游部39與入口管43,且在合流部47自上游部 39與出口管44合流。於合流部47設有混合閥34。 又,於熱交換器10中,宜使冷媒流路8之流動方向與 5 水流路9之流動方向相對,且緊密結合兩流路以使其間之 熱移動更為容易。藉由此構造使冷媒流路8與水流路9之 傳熱均勻,且熱交換效率更佳。並且,流出高溫熱水。发明 、 Explanation of the invention Yi Yi Leak § Fiber § Yi Fiber Fibrillation Jun: »» Fiber Inspection Keep the heat preservation part at a predetermined temperature. The hot water supply circuit 13 is branched from the branching portion 46 into an upstream portion 39 and an inlet pipe 43, and merges from the upstream portion 39 and the outlet pipe 44 at the joining portion 47. A mixing valve 34 is provided at the confluence part 47. In the heat exchanger 10, the flow direction of the refrigerant flow path 8 and the flow direction of the water flow path 9 should be opposite to each other, and the two flow paths should be closely combined to make the heat transfer between them easier. With this structure, the heat transfer between the refrigerant flow path 8 and the water flow path 9 is uniform, and the heat exchange efficiency is better. In addition, high-temperature hot water flows out.

又,儲存槽41的大小係以相當於因熱泵循環機構7或 熱交換器10供應熱水時之熱反應延遲而產生之不足的熱量 10 之蓄熱量來決定。例如,於給水溫度5°c且目標溫度45°c ,並以1 OL/min供應熱水時,若至目標溫度之熱水排出為 止延遲三分鐘,則不足熱量為(45 °C — 5 °C )xl0L/minx3min/860与 1.4kWh。以 80°C 之儲存槽 41 將其 補足時則為 1.4kWhx860/(80°C—5°C)=16L 之容量。 15 於給水管11係設有用以檢測熱水供應迴路13的流量The size of the storage tank 41 is determined based on the amount of stored heat equivalent to the amount of heat 10 that is insufficient due to the delay in the thermal reaction when the hot pump circulation mechanism 7 or the heat exchanger 10 supplies hot water. For example, when the feed water temperature is 5 ° c and the target temperature is 45 ° c, and hot water is supplied at 1 OL / min, if the delay of three minutes before the hot water is discharged from the target temperature, the insufficient heat is (45 ° C-5 ° C) x10L / minx3min / 860 and 1.4kWh. When it is replenished with the storage tank 41 at 80 ° C, it has a capacity of 1.4kWhx860 / (80 ° C-5 ° C) = 16L. 15 A water supply pipe 11 is provided to detect the flow of the hot water supply circuit 13

之流量檢測部20及用以檢測朝熱交換器10的給水溫度之 水溫檢測部21。並且,於熱水供應迴路13係設有用以檢 測流出熱水溫度之熱水溫度檢測部22。又,於儲存槽41 上部係設有用以檢測儲存槽41内的熱水溫度之儲存溫度檢 20 測部51。使用者係藉用以設定熱水供應的目標溫度之溫度 設定部23來任意地設定溫度。 控制部54 —旦藉由流量檢測部20檢測出流量,則從 熱水溫度檢測部22與溫度設定部23分別輸出之流出熱水 溫度與目標溫度之偏差鼻出反饋控制量。並且’從水溫檢 13 574491 r-./c ^:;; Λ;; ii;'a,::^i;r;^ l;:; 測部21與溫度設定部23與流量檢測部20之各值算出熱水 供應負荷。再將反饋控制量與熱水供應負荷相加,並根據 該相加值來控制壓縮機2之轉數。 又,控制部54係依照用以檢測氣溫之氣溫檢測部28 5 的檢測值來修正壓縮機2之轉數。又,分別控制減壓部4 、風扇32,且以最高效率運轉熱泵循環機構。於熱交換器 10之加熱量係與依照氣溫來變更壓縮機2之轉數成正比地 變化。於此,控制部54係預先記憶各氣溫之熱交換器10 的加熱量與壓縮機2之轉數的關係。然後,依照氣溫設定 10 控制轉數以使所需加熱量與熱交換器10之加熱量一致。藉 此,即使氣溫變動亦可高精度地控制熱水供應。 進而,控制部54驅動混合閥34,且控制來自熱水供 應迴路上游部39之流水與來自儲存槽41之流水的混合比 例,並使流出熱水溫度接近目標溫度。 15 又,控制部54於停止供應熱水時,由儲存溫度檢測部 51來檢測儲存溫度,且以低速旋轉控制壓縮機2以將儲存 溫度保持於預定溫度(例如80°C)並使其保溫運轉。藉由使 該保溫之預定溫度較熱水供應之目標溫度(例如45°C)高出 許多,可提高蓄熱密度。藉此,儲存槽25的尺寸可小型化 於以上之構造中,就其動作、作用加以說明。第1圖 中,若打開水龍頭17則自來水會從給水管11開始流入。 以流量檢測部20檢測之並將信號送至控制部54,而壓縮 機2開始運轉。此時,當熱泵循環機構7呈完全冷卻之狀 14 20 574491A flow rate detecting section 20 and a water temperature detecting section 21 for detecting a feed water temperature toward the heat exchanger 10. The hot water supply circuit 13 is provided with a hot water temperature detecting unit 22 for detecting the temperature of the outflowing hot water. Further, a storage temperature detecting section 51 for detecting the temperature of the hot water in the storage tank 41 is provided on the upper part of the storage tank 41. The user sets the temperature arbitrarily by the temperature setting unit 23 for setting the target temperature of the hot water supply. The control unit 54-once the flow rate is detected by the flow rate detection unit 20, the deviation of the outflowing hot water temperature from the hot water temperature detection unit 22 and the temperature setting unit 23 and the target temperature is output from the feedback control amount. And 'from water temperature inspection 13 574491 r-./c ^: ;; Λ ;; ii;' a, :: ^ i; r; ^ l;:; measuring section 21 and temperature setting section 23 and flow detection section 20 Each value calculates the hot water supply load. The feedback control amount is added to the hot water supply load, and the number of revolutions of the compressor 2 is controlled based on the added value. The control unit 54 corrects the number of revolutions of the compressor 2 based on the detection value of the air temperature detecting unit 28 5 for detecting the air temperature. In addition, the pressure reducing unit 4 and the fan 32 are controlled separately, and the heat pump cycle mechanism is operated at the highest efficiency. The amount of heating in the heat exchanger 10 changes in proportion to changing the number of revolutions of the compressor 2 in accordance with the temperature. Here, the control unit 54 previously memorizes the relationship between the heating amount of the heat exchanger 10 and the number of revolutions of the compressor 2 for each temperature. Then, the number of revolutions is controlled according to the air temperature setting 10 so that the required heating amount is consistent with the heating amount of the heat exchanger 10. This makes it possible to control hot water supply with high accuracy even if the temperature changes. Further, the control unit 54 drives the mixing valve 34, controls the mixing ratio of the flowing water from the hot water supply circuit upstream portion 39 and the flowing water from the storage tank 41, and brings the temperature of the outgoing hot water close to the target temperature. 15. When the control unit 54 stops supplying hot water, the storage temperature detection unit 51 detects the storage temperature, and controls the compressor 2 at a low speed to maintain the storage temperature at a predetermined temperature (for example, 80 ° C) and keep it warm. Running. By making the predetermined temperature of the insulation much higher than the target temperature of hot water supply (for example, 45 ° C), the heat storage density can be increased. Thereby, the size of the storage tank 25 can be miniaturized in the above structure, and its operation and effect will be described. In FIG. 1, when the faucet 17 is turned on, tap water will flow from the water supply pipe 11. The flow detection unit 20 detects this and sends a signal to the control unit 54, and the compressor 2 starts to operate. At this time, when the heat pump circulation mechanism 7 is completely cooled 14 20 574491

態時,即使運轉壓縮機2,循環機構整體之壓力與溫度亦 不會達到正常狀態,因此從水流路9會流出接近給水溫度 的水。控制部54係於開始供應熱水後之預定時間(例如三 分鐘)將混合閥34之混合比例設為例如1 : 1。於此,若給 5 水溫度5°C,儲存溫度80°C,且來自水流路9之出口溫度 仍為5°C,則混合閥34之出口溫度為(80°C +5°C)/2,即 42.5°C之流出熱水溫度。而後,水流路9之出口溫度會緩 緩地上升。但,儲存槽41内之儲存溫度由於從入口管43 流入接近給水溫度之冷水,故儲存槽41之出口溫度會緩緩 10 地下降。如此一來,混合閥34之出口溫度係維持混合有各 種流水而接近熱水供應之目標溫度(例如45°C)的溫度。 如上所述,混合閥34係控制成藉由在開始供應熱水後 立刻利用來自儲存槽41之熱水,以補充來自熱交換器10 之熱水供應延遲。且,在開始供應熱水時,當熱交換器10 15 之温度沒有變冷時,則從熱水溫度檢測部22輸出較目標溫 度高之值。此時係調整成上游部39側為多的混合比例且使 流出熱水溫度接近目標。 然後,熱泵循環機構7之溫度一旦穩定,則將混合闊 34之混合比例轉換至上游部39主體。此時,從壓縮機2 20 排出之高溫高壓的冷媒氣體係朝第1放熱器3A與第2放 熱器3流入,並加熱儲存槽41的水,且加熱流動於水流路 9中的水。然後,經加熱之水經過上游部3 9、熱水供應迴 路13而從熱水供應末端12流出。另一方面,於第1放熱 器3A與第2放熱器3冷卻之冷媒係藉減壓部4減壓並流 15 574491 發明說明 為Γ:£:4 入吸熱器5,於此,吸收大氣熱、太陽能等自然能量的熱 能而蒸發氣化,並返回壓縮機2。 於供應熱水中之控制部54係利用眾所皆知之比例一積 釀In the state, even if the compressor 2 is operated, the pressure and temperature of the entire circulation mechanism will not reach a normal state, and therefore water close to the feed water temperature will flow out from the water flow path 9. The control unit 54 sets the mixing ratio of the mixing valve 34 to, for example, 1: 1 at a predetermined time (for example, three minutes) after the hot water supply is started. Here, if the temperature of the water supply 5 is 5 ° C, the storage temperature is 80 ° C, and the outlet temperature from the water flow path 9 is still 5 ° C, then the outlet temperature of the mixing valve 34 is (80 ° C + 5 ° C) / 2, the temperature of the outgoing hot water at 42.5 ° C. Thereafter, the outlet temperature of the water flow path 9 will gradually rise. However, since the storage temperature in the storage tank 41 flows into the cold water close to the feed water temperature from the inlet pipe 43, the outlet temperature of the storage tank 41 will gradually decrease. In this way, the outlet temperature of the mixing valve 34 is maintained at a temperature close to the target temperature (for example, 45 ° C) of the hot water supply mixed with various flowing water. As described above, the mixing valve 34 is controlled to supplement the hot water supply delay from the heat exchanger 10 by using hot water from the storage tank 41 immediately after the hot water supply is started. Further, when the supply of hot water is started, if the temperature of the heat exchanger 10 15 does not become cold, a value higher than the target temperature is output from the hot water temperature detection unit 22. At this time, the mixing ratio is adjusted to be large on the upstream portion 39 side, and the temperature of the outflow hot water is brought close to the target. Then, once the temperature of the heat pump circulation mechanism 7 is stabilized, the mixing ratio of the mixer 34 is switched to the main body of the upstream portion 39. At this time, the high-temperature and high-pressure refrigerant gas system discharged from the compressor 2 20 flows into the first radiator 3A and the second radiator 3, heats the water in the storage tank 41, and heats the water flowing in the water flow path 9. Then, the heated water flows out from the hot water supply end 12 through the upstream portion 39 and the hot water supply circuit 13. On the other hand, the refrigerant cooled in the first heat radiator 3A and the second heat radiator 3 is decompressed and co-current by the decompression section 4 574491. The invention is described as Γ: £: 4 into the heat absorber 5, where it absorbs atmospheric heat. The heat energy of natural energy such as solar energy evaporates and gasifies, and returns to the compressor 2. The control unit 54 in the supply of hot water uses a well-known ratio

分一微分(PID)控制從流出熱水溫度與目標溫度之偏差算出 5 反饋控制量。此處的控制常數之比例增益或積分係數或微 分係數必須預先設定為可使控制之反應性與穩定性並存之 最適當的值。且,反饋控制為比例積分(PI)控制或者比例 (P)控制或者乏晰或類神經控制皆可。然後,另一方面,於 目標溫度與給水溫度之差乘上流量檢測部20所檢測之流量 10 以算出熱水供應負荷。此係所謂前饋控制量。然後,將反 饋控制量與前饋控制量相加,且利用該相加值來進行壓縮 機2之轉數控制。藉由加上該反饋控制,可將流出熱水溫 度正確地控制至目標溫度。特別是如PID控制或PI控制般 藉由利用積分要素,使流出熱水溫度更接近目標溫度。又 15 ,藉由使用比例控制要素,當剛開始供應熱水後等之流出 熱水溫度低時,由於以強大能力加熱控制故反應性良好。 另一方面,由於前饋控制為熱水供應之溫度穩定時的所需 熱量,故很少會有熱量過多或不足之情形且控制之穩定性 良好。又,當熱水供應流量或給水溫度急遽變化時,由於 20 直接反應且變更控制加熱量,故此點之反應性較反饋控制 佳而且穩定性好。然後,由於係將該反饋控制與前饋控制 相加來加以控制,故可活用各自的特徵且可達成反應性佳 並且穩定性良好之控制。 接著,就熱水供應停止時之動作加以說明。雖然儲存 16 574491The one-derivative (PID) control calculates the feedback control amount from the deviation of the outflow hot water temperature from the target temperature. The proportional gain, integral coefficient, or differential coefficient of the control constant must be set in advance to the most appropriate value that allows the reactivity and stability of the control to coexist. In addition, the feedback control may be proportional integral (PI) control or proportional (P) control or lack of or neural-like control. Then, on the other hand, the difference between the target temperature and the feed water temperature is multiplied by the flow rate 10 detected by the flow rate detection unit 20 to calculate the hot water supply load. This is the so-called feedforward control amount. Then, the feedback control amount and the feedforward control amount are added, and the added value is used to perform the revolution control of the compressor 2. By adding this feedback control, the outlet hot water temperature can be accurately controlled to the target temperature. In particular, by using integral elements such as PID control or PI control, the temperature of the outflow hot water is brought closer to the target temperature. Furthermore, by using the proportional control element, when the temperature of the hot water flowing out immediately after the hot water supply starts is low, the reactivity is good due to the powerful heating control. On the other hand, since the feedforward control is the amount of heat required when the temperature of the hot water supply is stable, there are rarely excessive or insufficient amounts of heat and the stability of the control is good. In addition, when the hot water supply flow or feed water temperature changes sharply, since 20 directly reacts and changes the control heating amount, the reactivity at this point is better than feedback control and the stability is good. Then, since the feedback control and the feedforward control are added together for control, the respective characteristics can be utilized, and control with good reactivity and stability can be achieved. Next, the operation when the hot water supply is stopped will be described. Although stored 16 574491

槽41以隔熱材料45覆蓋,但儲存溫度會因散熱而緩緩地 下降。控制部54係由儲存溫度檢測部51來檢測儲存溫度 。然後,若儲存溫度降至下限溫度(例如75°C)以下,則控 制壓縮機2以低速旋轉,且藉由第1放熱器3A加熱以使 5 儲存槽41内之溫度上升。此時,雖然亦加熱第2放熱器3 ,但由於在水流路9中,水並未流動,故一旦熱交換器10 是溫熱的,則不再吸取熱量。然後,若儲存溫度超過預定 溫度(例如80°C)則停止運轉壓縮機2。如此一來,可進行 保溫運轉以使儲存槽41之溫度保持於接近預定溫度。 10 又,雖然於本實施形態中係將第1放熱器3A設於儲 存槽41内部,但亦可構造成將放熱器捲繞在儲存槽41外 周等緊密結合於外周者。又,不利用第1放熱器3A,而是 藉由一般的加熱器來進行儲存槽41之保溫亦可。The tank 41 is covered with a heat-insulating material 45, but the storage temperature gradually decreases due to heat radiation. The control section 54 detects the storage temperature by the storage temperature detection section 51. Then, if the storage temperature falls below the lower limit temperature (for example, 75 ° C), the compressor 2 is controlled to rotate at a low speed and is heated by the first radiator 3A to increase the temperature in the storage tank 41. At this time, although the second radiator 3 is also heated, since water does not flow in the water flow path 9, once the heat exchanger 10 is warm, it no longer absorbs heat. Then, if the storage temperature exceeds a predetermined temperature (for example, 80 ° C), the operation of the compressor 2 is stopped. In this way, the temperature keeping operation can be performed to keep the temperature of the storage tank 41 close to a predetermined temperature. 10. Although the first radiator 3A is provided inside the storage tank 41 in this embodiment, the radiator may be structured such that the radiator is wound around the periphery of the storage tank 41 and tightly coupled to the periphery. In addition, instead of using the first radiator 3A, the storage tank 41 may be insulated by a general heater.

又,於本實施形態中,控制部54係控制成於開始供應 15 熱水時依照經過時間與混合溫度來變更混合閥34之混合比 例者。但,亦可以混合閥34為可變換儲存槽41的流水與 熱水供應迴路上游部3 9的流水之變換閥。此時一旦儲存槽 41之儲存溫度設定成熱水供應之目標溫度,且來自水流路 9之出口溫度上升至接近目標溫度,則控制成將流水從儲 20 存槽41變換至上游部39。依此構造,相較於混合閥34, 變換閥為較簡易之機構且容易控制,並適合低成本化。 又,於本實施形態之熱水供應裝置中,熱泵循環機構 7為冷媒壓力在臨界壓力以上之超臨界熱泵循環機構。而 且,藉由升壓至臨界壓力以上之冷媒來加熱熱交換器10之 17 574491 玖、發明說明 漏緣靈纖»^懸纖綴ββϋ孩In the present embodiment, the control unit 54 controls the mixing ratio of the mixing valve 34 to be changed in accordance with the elapsed time and the mixing temperature when hot water supply is started. However, the mixing valve 34 may be a switching valve for switching the flowing water in the storage tank 41 and the flowing water in the hot water supply circuit upstream portion 39. At this time, once the storage temperature of the storage tank 41 is set to the target temperature of the hot water supply, and the outlet temperature from the water flow path 9 rises to near the target temperature, it is controlled to change the flowing water from the storage 20 storage tank 41 to the upstream portion 39. According to this structure, compared with the mixing valve 34, the change-over valve is a simpler mechanism, is easy to control, and is suitable for cost reduction. In the hot water supply device according to this embodiment, the heat pump circulation mechanism 7 is a supercritical heat pump circulation mechanism having a refrigerant pressure equal to or higher than a critical pressure. In addition, the heat exchanger 10 is heated by a refrigerant that is raised above a critical pressure. 17 574491 发明, description of the invention

水流路9的流水。流動於熱交換器10之冷媒流路8的冷媒 係由於藉壓縮機2加壓至臨界壓力以上,故即使被水流路 9之流水將熱奪去而溫度下降亦不會凝結。因此,於熱交 換器10整個領域中,在冷媒流路8與水流路9容易形成溫 5 度差,並可得到高溫熱水,且可提高熱交換效率。但,亦 可使用一般的臨界壓力以下之熱泵循環機構。此在下述之 各實施形態中亦相同。Flowing water in the water flow path 9. Since the refrigerant flowing in the refrigerant flow path 8 of the heat exchanger 10 is pressurized to a pressure above the critical pressure by the compressor 2, the temperature will not be condensed even if the heat is taken away by the flowing water in the water flow path 9 and the temperature drops. Therefore, in the entire field of the heat exchanger 10, a temperature difference of 5 degrees is easily formed between the refrigerant flow path 8 and the water flow path 9, high-temperature hot water can be obtained, and heat exchange efficiency can be improved. However, it is also possible to use a general heat pump circulation mechanism below the critical pressure. This is the same in each embodiment described below.

又,於本實施形態之熱水供應裝置中,在熱交換器10 中,冷媒流路8之流動方向與水流路9之流動方向係相對 10 。藉此,於熱交換器10中,冷媒流路8與冷媒流路9之傳 熱可均勻,且熱交換效率佳並可流出高溫熱水。此在下述 之各實施形態中亦相同。 (第2實施形態)In the hot water supply device of this embodiment, in the heat exchanger 10, the flow direction of the refrigerant flow path 8 and the flow direction of the water flow path 9 are opposite to each other. Thereby, in the heat exchanger 10, the heat transfer between the refrigerant flow path 8 and the refrigerant flow path 9 can be uniform, the heat exchange efficiency is good, and high-temperature hot water can flow out. This is the same in each of the following embodiments. (Second Embodiment)

第2圖係本發明第2實施形態之熱泵式熱水供應裝置 15 的構成圖。第2圖中,與第1實施形態之構成不同之處為 設有取代加溫部38之加溫部60。加溫部60係構造成設有 與熱水供應迴路13排成一列之蓄熱部61。另一不同點是 蓄熱部61將入口管63配置於儲存槽62上部且於儲存槽 62内部混合儲存槽62的熱水與來自熱交換器的水(熱水)。 20 而且,將儲存槽62進行保溫運轉時之儲存溫度設為與熱水 供應之目標溫度(例如45°C)相同之溫度。但,若儲存溫度 低,則儲存槽62之容量要大。 於以上之構造中,若從熱交換器10完全冷卻之狀態開 始供應熱水,則接近給水溫度之冷水會從入口管63流入儲 18 574491Fig. 2 is a configuration diagram of a heat pump hot water supply device 15 according to a second embodiment of the present invention. In Fig. 2, a difference from the first embodiment is that a heating portion 60 is provided instead of the heating portion 38. The heating section 60 is configured to include a heat storage section 61 aligned with the hot water supply circuit 13. Another difference is that the heat storage unit 61 arranges the inlet pipe 63 on the upper part of the storage tank 62 and mixes the hot water from the storage tank 62 and the water (hot water) from the heat exchanger inside the storage tank 62. 20 Furthermore, the storage temperature during the holding operation of the storage tank 62 is set to the same temperature as the target temperature (for example, 45 ° C) for hot water supply. However, if the storage temperature is low, the capacity of the storage tank 62 becomes large. In the above configuration, if hot water is supplied from the state where the heat exchanger 10 is completely cooled, cold water close to the feed water temperature will flow into the storage 18 from the inlet pipe 63.

纖:戀^^纖錄沒驗驗凝纖纖鐵疆凝纖鐵鐵體鑛輝:纖:_:簿從^^ 玖、發明說明Fiber: Lian ^^ Fiber Records Examination of Condensed Fiber Fiber Iron Xinjiang Condensed Fiber Iron Ferrite Ore: Fiber: _: 书 从 ^^ 发明, Description of the Invention

存槽62。如此一來,於儲存槽62内部,從與内部之溫水 的溫度差看來,流入的水會流入儲存槽62底部,而僅裡面 的溫水會出口管44流出。因此,從開始供應熱水後立刻可 流出接近熱水供應之目標溫度的熱水。若從入口管63流入 5 之溫度上升,則會於儲存槽62内與上部之溫水混合並從出 口管44流出。又,當流出較儲存溫度高溫之熱水時,較儲 存溫度高溫之熱水會從入口管63流入儲存槽62。此時, 由於所流入之熱水的比重輕,故會流至儲存槽62上端,且 仍舊從出口管44流出。如此一來,於儲存槽62内部可進 10 行熱水與水之變換混合。 如上所述,於本實施形態中,正因為將蓄熱部61直列 地連接於熱水供應迴路13,而可彌補開始供應熱水時之熱 水供應延遲並實現穩定的溫度之熱水供應。又,由於在儲 存槽62内部可自然且適溫地混合,故不需要混合部而可降 15 低成本。存 槽 62。 Storage slot 62. In this way, from the perspective of the temperature difference from the warm water inside the storage tank 62, the inflowing water will flow into the bottom of the storage tank 62, and only the warm water inside will flow out of the outlet pipe 44. Therefore, immediately after the hot water supply is started, hot water close to the target temperature of the hot water supply can flow out. If the temperature of the inflow 5 from the inlet pipe 63 rises, it will mix with the warm water in the upper part in the storage tank 62 and flow out from the outlet pipe 44. When hot water having a higher temperature than the storage temperature flows out, hot water having a higher temperature than the storage temperature flows from the inlet pipe 63 into the storage tank 62. At this time, since the specific gravity of the hot water flowing in is light, it flows to the upper end of the storage tank 62 and still flows out of the outlet pipe 44. In this way, 10 rows of hot water and water can be mixed in the storage tank 62. As described above, in the present embodiment, the heat storage unit 61 is connected to the hot water supply circuit 13 in series, so that the hot water supply delay at the start of hot water supply can be made up and the hot water supply at a stable temperature can be realized. In addition, since the mixture can be naturally and appropriately mixed in the storage tank 62, a mixing section is not required, and the cost can be reduced.

(第3實施形態) 第3圖係本發明第3實施形態之熱泵式熱水供應裝置 的構成圖。第3圖中,與第2實施形態之構成不同之處為 設有取代加溫部60之加溫部70。加溫部70係構造成設有 20 與給水管11排成一列之蓄熱部71。另一不同點是蓄熱部 71將入口管73配置於儲存槽72底部。而且,將儲存槽72 進行保溫運轉時之儲存溫度設為與熱水供應之目標溫度(例 如45t)相同之溫度。 於以上之構造中,若從熱交換器10完全冷卻之狀態開 19 574491 始供應熱水,則冷水會從給水管11流入儲存槽72底部, 且儲存槽72之溫水會從出口管44流出。然後,當增加熱 交換器10之加熱量時,係藉由熱水溫度檢測部22之檢測 溫度來控制壓縮機2之轉數,並維持目標溫度之流出熱水 溫度。(Third Embodiment) Fig. 3 is a configuration diagram of a heat pump-type hot water supply device according to a third embodiment of the present invention. In Fig. 3, a difference from the configuration of the second embodiment is that a heating section 70 is provided instead of the heating section 60. The heating section 70 is configured to have a heat storage section 71 arranged in a line with the water supply pipe 11. Another difference is that the heat storage section 71 arranges the inlet pipe 73 at the bottom of the storage tank 72. Furthermore, the storage temperature during the holding operation of the storage tank 72 is set to the same temperature as the target temperature (e.g., 45t) of hot water supply. In the above structure, if hot water is supplied from 19 574491 when the heat exchanger 10 is completely cooled, cold water will flow from the water supply pipe 11 to the bottom of the storage tank 72, and warm water from the storage tank 72 will flow out from the outlet pipe 44 . Then, when the heating amount of the heat exchanger 10 is increased, the number of revolutions of the compressor 2 is controlled by the temperature detected by the hot water temperature detecting section 22, and the outflow hot water temperature at the target temperature is maintained.

如上所述,於本實施形態中,係於熱交換器10之上游 側配置有蓄熱部71。藉此,當熱交換器10之加熱延遲時 ,蓄熱部71則予以補充。當熱交換器10之加熱能力升高 時,則藉由流出熱水溫度之反饋控制來控制壓縮機2,且 10 通常可維持目標之熱水供應溫度。又,即使變更目標溫度 ,亦可立刻改變流出熱水溫度。 再者,由於在開始供應熱水時,藉由儲存槽72之溫水 來溫熱熱交換器10,故熱泵循環機構7之溫度升高速度亦 變快。 15 又,於本實施形態中,係構造成使蓄熱部71與給水管As described above, in the present embodiment, the heat storage section 71 is arranged upstream of the heat exchanger 10. Thus, when the heating of the heat exchanger 10 is delayed, the heat storage section 71 is supplemented. When the heating capacity of the heat exchanger 10 increases, the compressor 2 is controlled by the feedback control of the temperature of the hot water flowing out, and 10 can usually maintain the target hot water supply temperature. In addition, even if the target temperature is changed, the outflow hot water temperature can be changed immediately. Furthermore, since the heat exchanger 10 is warmed by the warm water in the storage tank 72 when hot water supply is started, the temperature of the heat pump circulation mechanism 7 is also increased at a faster rate. 15 In this embodiment, the heat storage unit 71 and the water supply pipe are configured

11排成一列。但,若與給水管11並列地配置,且將儲存 溫度設為較熱水供應之目標溫度高,並將給水管11的流水 與蓄熱部的溫水混合成接近目標溫度的溫度,並且使其流 至熱交換器10,則因高溫蓄熱,蓄熱部71可小型化。 20 又,於第1、第2實施形態中係將蓄熱部配置於熱交 換器10之下游,而於第3實施形態則配置於上游。但,亦 可並列地配置蓄熱部以與熱交換器10並聯,亦可在熱交換 器10之上游側配置蓄熱部,以混合水流路11的流水與蓄 熱部的流水。再者,即使配置成於蓄熱部内藏熱交換器10 20 574491 誦圓 ίΧ'發明說明 亦可得到同樣的效果。 (第4實施形態) 第4圖係本發明第4實施形態之熱泵式熱水供應裝置 的構成圖。第4圖中,與第1實施形態之構成不同之處為 5 設有取代加溫部38之加溫部80。加溫部80係由包含水流 路9而形成之水循環路81及配置於水循環路81上之蓄熱 部82所構成。然後,為了保持水循環路81與蓄熱部82之 循環水的溫度,係驅動熱泵循環機構7且加熱熱交換器10 之水流路9,並於水循環路81產生自然對流。蓄熱部82 10 係由上下配置有入口管43與出口管44之儲存槽83及用以 混合來自出口管44的流水與來自水流路9的流水且使其流 至熱水供應迴路13之混合閥34所構成。水循環路81係構 造成將水流路9與混合閥34與儲存槽83連通成環狀者。 於以上之構造中,若從熱交換器10完全冷卻之狀態開 15 始供應熱水,則冷水會從給水管11流入水流路9與儲存槽 83,且來自水流路9的出口之冷水與來自儲存槽83之溫水 會藉混合閥34混合並流至熱水供應迴路13。此時,由於 藉由熱水溫度檢測部22之檢測溫度來決定混合閥34之開 啟度,故流至熱水供應迴路13之熱水溫度會控制於目標溫 20 度。然後,當增加熱交換器10之加熱量時,係藉由熱水溫 度檢測部22之檢測溫度來減少從儲存槽83流出之熱水比 例。若從水流路9流出之熱水溫度達到目標溫度,則停止 從儲存槽83流出熱水。 當停止供應熱水時,儲存槽83内之蓄熱量會因供應熱 21 57449111 in a row. However, if it is arranged in parallel with the water supply pipe 11 and the storage temperature is set to be higher than the target temperature of hot water supply, the flowing water of the water supply pipe 11 and the hot water in the heat storage section are mixed to a temperature close to the target temperature and the When flowing to the heat exchanger 10, the heat storage section 71 can be miniaturized due to high-temperature heat storage. 20 In the first and second embodiments, the heat storage unit is disposed downstream of the heat exchanger 10, and in the third embodiment, it is disposed upstream. However, the heat storage section may be arranged in parallel with the heat exchanger 10, or the heat storage section may be arranged upstream of the heat exchanger 10 to mix the flow of water from the water flow path 11 and the flow of the heat storage section. In addition, the same effect can be obtained even if the heat exchanger 10 20 574491 is arranged in the heat storage section. (Fourth Embodiment) Fig. 4 is a configuration diagram of a heat pump-type hot water supply device according to a fourth embodiment of the present invention. In Fig. 4, a difference from the first embodiment is that a heating portion 80 is provided instead of the heating portion 38. The heating section 80 is composed of a water circulation path 81 formed by including the water flow path 9 and a heat storage section 82 disposed on the water circulation path 81. Then, in order to maintain the temperature of the circulating water in the water circulation path 81 and the heat storage unit 82, the water flow path 9 of the heat exchanger 10 is driven by heating the heat pump circulation mechanism 7 and generating natural convection in the water circulation path 81. The heat storage unit 82 10 is a storage tank 83 having an inlet pipe 43 and an outlet pipe 44 arranged above and below, and a mixing valve for mixing the flowing water from the outlet pipe 44 and the flowing water from the water flow path 9 and flowing the hot water supply circuit 13 34. The water circulation path 81 is structured such that the water flow path 9 and the mixing valve 34 and the storage tank 83 communicate with each other in a ring shape. In the above structure, if hot water is supplied from 15 when the heat exchanger 10 is completely cooled, cold water will flow from the water supply pipe 11 into the water flow path 9 and the storage tank 83, and cold water from the outlet of the water flow path 9 and from The warm water in the storage tank 83 is mixed by the mixing valve 34 and flows to the hot water supply circuit 13. At this time, since the opening degree of the mixing valve 34 is determined by the detection temperature of the hot water temperature detecting section 22, the temperature of the hot water flowing to the hot water supply circuit 13 is controlled to a target temperature of 20 degrees. Then, when the heating amount of the heat exchanger 10 is increased, the proportion of hot water flowing out of the storage tank 83 is reduced by the temperature detected by the hot water temperature detecting section 22. When the temperature of the hot water flowing out of the water flow path 9 reaches the target temperature, the hot water flowing out of the storage tank 83 is stopped. When the supply of hot water is stopped, the amount of heat stored in the storage tank 83 will be due to the supply of heat 21 574491

% 發明說明% Invention Description

讀雜纏_編Reading miscellaneous

_ 、?、> 、、·、、< Ά、'•S'·、、、、_,?, ≫,, · ,, < Ά, '• S' · ,,,,

水時所流入之給水而下降。於此,控制部54係首先使混合 閥34回到混合狀態。然後,一旦藉由儲存溫度檢測部51 檢測出儲存溫度下降(例如75°C以下),則驅動熱泵循環機 構7,且運轉壓縮機2以低速旋轉。藉此,高溫高壓之冷 5 媒係流至冷媒流路8,且加熱水流路9。若水流路9中之水 溫上升且較儲存槽83内之水溫高,則因兩者之溫度差,水 流路9内的水會上升,而於水循環路81内產生對流。而且 ,若儲存槽83内之溫度上升,且儲存溫度檢測部51之檢 測溫度超過預定溫度(例如80°C),則停止運轉熱泵循環機 10 構7。藉由反覆該運轉及停止,可保持蓄熱部82與水循環 路81之循環水的溫度。When the water flows in, it drops. Here, the control unit 54 first returns the mixing valve 34 to the mixing state. When the storage temperature detection unit 51 detects a decrease in the storage temperature (for example, 75 ° C or lower), the heat pump cycle mechanism 7 is driven and the compressor 2 is rotated at a low speed. Thereby, the high-temperature and high-pressure refrigerant 5 flows to the refrigerant flow path 8 and heats the water flow path 9. If the water temperature in the water flow path 9 rises and is higher than the water temperature in the storage tank 83, the water in the water flow path 9 rises due to the temperature difference between the two, and convection occurs in the water circulation path 81. Further, if the temperature in the storage tank 83 rises and the temperature detected by the storage temperature detecting section 51 exceeds a predetermined temperature (for example, 80 ° C), the heat pump cycle machine 10 is stopped. By repeating this operation and stopping, the temperatures of the circulating water in the heat storage unit 82 and the water circulation path 81 can be maintained.

以上,根據第4實施形態之構造,係保持水流路9及 包含蓄熱部82之水循環路81的溫度,且於開始供應熱水 時使水循環路81的熱水流出。因而,從熱水供應末端12 15 流出之熱水的溫度升高會變快。又,由於在停止熱泵循環 機構7時,水循環路81的熱會溫熱熱交換器10,故熱泵 循環機構7之溫度升高亦會變快。 又,由於藉由熱泵來進行水循環路81之保溫,故相較 於加熱器等,其效率佳,且無結冰之虞。 20 再者,由於在蓄熱部82儲存高溫熱水,且藉混合閥 34混合成適溫而流出熱水,故即使在開始供應熱水時冷水 流入水循環路81,亦可防止流出熱水溫度過低。 又,雖然於本實施形態中在保溫運轉中之水循環路81 内的水循環係利用因自然對流而產生之流水,但亦可於水 22 574491 麵摄纖觀篸轉毅;纖 棚母Η日 ι Jiwt Μ 循環路81設置泵,而強制性地使流水循環。此時由於可獲 得穩定的流量,故容易控制儲存溫度與在熱交換器之加熱 熱量。As described above, according to the structure of the fourth embodiment, the temperature of the water flow path 9 and the water circulation path 81 including the heat storage section 82 is maintained, and the hot water of the water circulation path 81 is caused to flow out when hot water supply is started. Therefore, the temperature of the hot water flowing out from the hot water supply end 12 15 becomes faster. In addition, when the heat pump circulation mechanism 7 is stopped, the heat of the water circulation path 81 warms the heat exchanger 10, so that the temperature of the heat pump circulation mechanism 7 also increases quickly. In addition, since the water circulation path 81 is insulated by a heat pump, the efficiency is better than that of a heater or the like, and there is no risk of freezing. 20 Furthermore, since high-temperature hot water is stored in the heat storage unit 82, and the hot water flows out by mixing with the mixing valve 34 to an appropriate temperature, even if cold water flows into the water circulation path 81 when hot water starts to be supplied, the temperature of the hot water flowing out can be prevented low. In addition, although the water circulation in the water circulation path 81 during the heat preservation operation in this embodiment uses the flowing water generated by natural convection, the fiber can also be viewed at the water 22 574491 surface; The Jiwt M circulation circuit 81 is provided with a pump to circulate the flowing water forcibly. At this time, since a stable flow rate can be obtained, it is easy to control the storage temperature and the heating heat in the heat exchanger.

又,雖然於本實施形態中係藉由混合閥34使混合比例 5 改變,但亦可以固定於一定比例之合流構件來構成。此時 必須藉由壓縮機2來控制熱交換器10之加熱量以配合儲存 槽83之熱水的減少而使流出熱水溫度達到目標溫度。根據 該構造,由於係使用簡便的混合閥34,故可降低成本。 再者,雖然於本實施形態中係將蓄熱部82配置於水循 10 環路81,但即使是沒有蓄熱部82之水循環路81的構造亦 可。此時係配置成藉由儲存溫度檢測部51來檢測水循環路 81之循環水的溫度,且進行保溫運轉以將循環水之溫度保 持於預定溫度。依該構造,雖然流出熱水溫度會稍微變動 ,但不需要蓄熱部82,而可大幅降低成本。 15 於本實施形態中係藉由驅動熱泵循環機構7且加熱熱In addition, although the mixing ratio 5 is changed by the mixing valve 34 in the present embodiment, it may be constructed by fixing to a merging member of a certain ratio. At this time, the heating amount of the heat exchanger 10 must be controlled by the compressor 2 so as to cooperate with the reduction of the hot water in the storage tank 83 so that the temperature of the outgoing hot water reaches the target temperature. According to this structure, since the mixing valve 34 is simple to use, the cost can be reduced. Furthermore, although the heat storage section 82 is arranged in the water circulation loop 81 in this embodiment, the structure of the water circulation path 81 without the heat storage section 82 may be used. At this time, it is configured to detect the temperature of the circulating water in the water circulation path 81 by the storage temperature detecting section 51, and perform a heat preservation operation to maintain the temperature of the circulating water at a predetermined temperature. With this structure, although the temperature of the outflow hot water fluctuates slightly, the heat storage unit 82 is not required, and the cost can be significantly reduced. 15 In this embodiment, the heat pump circulation mechanism 7 is driven and the heat is heated.

交換器10之水流路9,而於水循環路81產生自然對流並 加熱保溫之。如此一來,由於藉由熱泵來進行水循環路之 保溫,故相較於加熱器等,其效率佳,又,由於在保溫時 驅動熱果循壞機構7 ’故熱栗循5哀機構7本身的溫度升南 20 速度亦變快。又,亦可直接以加熱器加熱水循環路81,亦 可直接以加熱器加熱儲存槽83。 又,在平常的熱水供應使用狀態下,冷媒流路8與水 流路9之溫度差愈小,熱泵循環機構7之效率則愈好。因 此,若依照水溫檢測部21所檢測之給水溫度,且確保在熱 23 574491The water flow path 9 of the exchanger 10 generates natural convection in the water circulation path 81 and heats it to keep it warm. In this way, heat preservation of the water circulation path is performed by a heat pump, so the efficiency is better than that of a heater, etc., and because the heat-recycling mechanism 7 is driven during heat preservation, the heat-recycling mechanism 5 itself The temperature rose 20 south faster. The water circulation path 81 may be directly heated by a heater, or the storage tank 83 may be directly heated by a heater. In addition, in a normal hot water supply and use state, the smaller the temperature difference between the refrigerant flow path 8 and the water flow path 9, the better the efficiency of the heat pump circulation mechanism 7. Therefore, if the feed water temperature detected by the water temperature detection unit 21 is followed,

玖、發明說明 交換器10之所需加熱量,並控制減壓部4之冷媒流路阻力 以使冷媒流路8與水流路9之溫度差減到最小,則可進行 高效率之運轉。发明 Description of the invention The required heating amount of the exchanger 10 and the resistance of the refrigerant flow path of the decompression section 4 are controlled so as to minimize the temperature difference between the refrigerant flow path 8 and the water flow path 9, so that high-efficiency operation can be performed.

根據第1至第4實施形態,由於除了以熱交換器加熱 5 自來水以外亦以加溫部加熱,故即使在熱交換器之加熱不 充分,亦可補其不足而藉加溫部來加熱。又,由於加溫部 不會直接影響由熱交換器進行之熱水溫度控制,故控制性 佳。再者,由於冷媒與水之熱交換係與加溫部無關而以熱 交換器來進行,故可進行高效率之熱交換。又,由於蓄熱 10 部之熱水係保持於預定溫度,故即使在壓縮機或熱交換器 完全冷卻之狀態下開始供應熱水,由於藉由蓄熱部之熱水 來加熱給水管與熱交換器與熱水供應迴路之其中一者的水 ,故流出熱水溫度之升高速度可非常快速。又,由於藉由 熱泵來進行蓄熱部之保溫,故相較於加熱器等,其效率佳 15 ,又,由於在保溫時驅動熱泵循環機構,故在開始供應熱 水時之溫度升高速度會變快。又,由於保持給水管與水流 路與熱水供應迴路之至少一者的溫度,故在開始供應熱水 時,水循環路之熱水會流出,且溫度升高速度會變快。又 ,由於水循環路之熱會溫熱熱交換器,故熱栗循環機構之 20 溫度升高速度亦很快。又,由於蓄熱部的尺寸相當合適, 故無蓄熱部過大而增加散熱損耗,且設置空間或重量變大 等問題。再者,因使蓄熱部之熱水溫度較熱水供應温度高 ,而提高蓄熱密度,因而縮小蓄熱部尺寸,藉此可減少設 置空間與重量。又,以熱水供應所使用的水作為蓄熱部來 24 574491 Λ'^ '' ί,'V,\; ;,-, '; ^ ^ Λ ^ ^ ^ 佶用,莊少A、s β 从 使用精此在&通’右抽出水則可減輕重量。又,作為 蓄熱材料,其比熱大,而且安全 又,若使用超臨界熱系循環機構,則流動於熱交換器 5 之冷媒流路的冷媒會藉壓縮機加壓至臨界壓力以上。因而 ,即使因熱交換H之水流路的流水將熱奪走而溫度降低亦 不會凝結。目此,於熱交換詩_射,在冷媒流路與 水流路容易形成溫度差,並可得到高溫熱水,且可提高熱 交換效率。According to the first to fourth embodiments, in addition to heating the tap water in the heat exchanger, the heating section is used for heating. Therefore, even if the heating in the heat exchanger is insufficient, it can be supplemented by the heating section for heating. In addition, since the heating section does not directly affect the hot water temperature control by the heat exchanger, the controllability is excellent. Furthermore, since the heat exchange system between the refrigerant and water is performed by a heat exchanger regardless of the heating section, high-efficiency heat exchange can be performed. In addition, since the hot water of the 10 heat storage units is maintained at a predetermined temperature, the hot water supply is started even when the compressor or the heat exchanger is completely cooled. The hot water supply pipe and the heat exchanger are heated by the hot water of the heat storage unit. And hot water supply circuit, so the temperature of outflow hot water can increase very quickly. In addition, because the heat storage unit is insulated by a heat pump, its efficiency is better than that of a heater, etc.15, and because the heat pump circulation mechanism is driven during the heat preservation, the temperature rise rate at the beginning of hot water supply Get faster. In addition, since the temperature of at least one of the water supply pipe, the water flow path, and the hot water supply circuit is maintained, when the hot water supply is started, the hot water in the water circulation path flows out and the temperature rises faster. In addition, since the heat of the water circulation path warms the heat exchanger, the temperature rise rate of the heat pump circulation mechanism is also fast. In addition, since the size of the heat storage section is quite suitable, there is no problem that the heat storage section is too large to increase heat dissipation loss, and the installation space or weight becomes large. Furthermore, since the hot water temperature of the heat storage section is higher than the hot water supply temperature, the heat storage density is increased, so the size of the heat storage section is reduced, thereby reducing the installation space and weight. In addition, the water used for hot water supply is used as a heat storage unit to 24 574491 Λ '^' 'ί,' V, \;; ,,, ;; ^ ^ Λ ^ ^ ^ 佶, Zhuang Shao A, s β from You can save weight by pumping water on the right. As a heat storage material, its specific heat is large, and it is safe. When a supercritical thermal system circulation mechanism is used, the refrigerant flowing in the refrigerant flow path of the heat exchanger 5 is pressurized to a critical pressure or higher by a compressor. Therefore, even if the temperature is lowered due to the heat being taken away by the flowing water in the water flow path of the heat exchange H, the condensation does not occur. For this reason, in the heat exchange poem, the temperature difference between the refrigerant flow path and the water flow path is easy to form, and high-temperature hot water can be obtained, and the heat exchange efficiency can be improved.

又,根據第1、第4實施形態,係藉由改變蓄熱部側 1〇之流量,而可自由地設定藉由蓄熱部之熱來加熱給水管與 熱交換器與熱水供應迴路之其中一者的水之熱量。又,由 於來自蓄熱部的熱水可與給水管和熱交換器和熱水供應迴 路之其中者的水以預定比例混合加熱,故可立刻得到預 定之流出熱水溫度。又,由於可變換來自蓄熱部的熱水與 15給水管和熱交換器和熱水供應迴路之其中一者的水並使其 流動,故當開始供應熱水時或除霜時等來自熱交換器之加 熱不足時,可利用來自蓄熱部的熱水,而不會令使用者感 到不滿意。 (第5實施形態) 2〇 第5圖係本發明第5實施形態之熱泵式熱水供應裝置 的構成圖。第5圖中,於熱泵循環機構7中係藉由冷媒流 路1將壓縮機2、放熱器3、減壓部4及吸熱器5連接成閉 路。熱交換器10係具有用以與放熱器3之冷媒流路8進行 熱父換之水流路9。用以將自來水直接供給至水流路9之 25 574491 發明說明 籍謙讎 g纖鍵鱗釋In addition, according to the first and fourth embodiments, one of the water supply pipes, the heat exchanger, and the hot water supply circuit can be freely set to be heated by the heat of the heat storage section by changing the flow rate of the heat storage section 10. Heat of water. In addition, since the hot water from the heat storage section can be mixed with the water in the water supply pipe, the heat exchanger, and the hot water supply circuit in a predetermined ratio, the predetermined hot water temperature can be obtained immediately. In addition, the hot water from the heat storage unit and the water from one of the 15 water supply pipe, the heat exchanger, and the hot water supply circuit can be changed and flowed. Therefore, when the hot water supply is started or the defrosting is started, the heat exchange is performed When the heating of the device is insufficient, hot water from the heat storage section can be used without dissatisfaction of the user. (Fifth Embodiment) Fig. 5 is a configuration diagram of a heat pump-type hot water supply device according to a fifth embodiment of the present invention. In Fig. 5, in the heat pump cycle mechanism 7, the compressor 2, the radiator 3, the pressure reducing section 4, and the heat absorber 5 are connected to each other via a refrigerant flow path 1 in a closed circuit. The heat exchanger 10 has a water flow path 9 for heat exchange with the refrigerant flow path 8 of the radiator 3. Used to supply tap water directly to water channel 9 25 574491 Description of the invention Ji Qiang g fiber key scale release

給水管11係與可使從水流路9流出之熱水通水至由蓮蓬頭 16或水龍頭17等所構成之熱水供應末端12之熱水供應迴 路13相連接。而且,負荷設定部18係用以設定於熱交換 器10之所需加熱量。加熱控制部19係依照負荷設定部18 5 之設定值來控制熱交換器10之加熱量。於給水管11係設 有用以檢測熱水供應迴路13的流量之流量檢測部20及用 以檢測朝熱交換器10的給水溫度之水溫檢測部21。於熱 水供應迴路13係設有用以檢測來自水流路9的流出熱水溫 度之熱水溫度檢測部22。使用者係藉用以設定熱水供應的 10 目標溫度之溫度設定部23來任意地設定溫度。The water supply pipe 11 is connected to a hot water supply circuit 13 that allows hot water flowing out of the water flow path 9 to pass through to a hot water supply terminal 12 composed of a shower head 16 or a faucet 17 or the like. The load setting unit 18 is used to set a required heating amount in the heat exchanger 10. The heating control unit 19 controls the heating amount of the heat exchanger 10 in accordance with the setting value of the load setting unit 18 5. The water supply pipe 11 is provided with a flow rate detection unit 20 for detecting the flow rate of the hot water supply circuit 13, and a water temperature detection unit 21 for detecting the temperature of the water supply to the heat exchanger 10. The hot water supply circuit 13 is provided with a hot water temperature detecting unit 22 for detecting the temperature of the hot water flowing out from the water flow path 9. The user sets the temperature arbitrarily by using the temperature setting unit 23 for setting the target temperature of the hot water supply.

負荷設定部18係包含有第1算定部24、第2算定部 25及加算部26。第1算定部24係從熱水溫度檢測部22與 溫度設定部23分別輸出之流出熱水溫度與目標溫度之偏差 算出第1所需加熱量。第2算定部25係從水溫檢測部21 15 與溫度設定部23與流量檢測部20之各值算出第2所需加 熱量。加算部26係將第1所需加熱量與第2所需加熱量相 加。負荷設定部18係輸出經相加之所需加熱量。 加熱控制部19係具有用以變更壓縮機2的轉數之頻率 控制部27,且依照由負荷設定部18所設定之所需加熱量 20 來控制壓縮機2之轉數。 加熱控制部19係依照用以檢測氣溫之氣溫檢測部28 的檢測值來變更熱泵循環機構的運轉條件之壓縮機2的轉 數且控制熱交換器之加熱量。於熱交換器10之加熱量係與 依照氣溫來變更壓縮機2之轉數成正比地變化。因此,加 26 574491The load setting unit 18 includes a first calculation unit 24, a second calculation unit 25, and an addition unit 26. The first calculation unit 24 calculates a first required heating amount from the deviation between the outflow hot water temperature and the target temperature output by the hot water temperature detection unit 22 and the temperature setting unit 23, respectively. The second calculation unit 25 calculates the second required heating amount from each value of the water temperature detection unit 21 15, the temperature setting unit 23, and the flow rate detection unit 20. The adding unit 26 adds the first required heating amount and the second required heating amount. The load setting unit 18 outputs the required heating amount after the addition. The heating control unit 19 includes a frequency control unit 27 for changing the number of revolutions of the compressor 2, and controls the number of revolutions of the compressor 2 in accordance with the required heating amount 20 set by the load setting unit 18. The heating control unit 19 changes the rotation speed of the compressor 2 and controls the heating amount of the heat exchanger in accordance with the detection value of the air temperature detecting unit 28 for detecting the air temperature. The amount of heating in the heat exchanger 10 changes in proportion to changing the number of revolutions of the compressor 2 in accordance with the temperature. Therefore, add 26 574491

熱控制部19係預先記憶各氣溫之熱交換器1〇的加熱量與 壓縮機2之轉數的關係。然後,依照氣溫來設定控制轉數 ,以使由負荷設定部18所設定之所需加熱量與熱交換器 10之加熱量一致。藉此,即使氣溫變動亦可高精度地進行 5 熱水供應控制。 又’負荷設定部18與加熱控制部19係構造成相當於 第1至第4實施形態的控制部54之控制部29。該等控制 部亦可一體地構成。 · 於以上之構造中,就其動作、作用加以說明。第5圖 1〇中,若打開水龍頭Π則自來水會從給水管u開始流入。 以流量檢測部20檢測之並將信號送至負荷設定部18。負 荷設定部18係算出所需加熱量,且加熱控制部19係根據 該算定值來控制壓縮機2之轉數。然後,從壓縮機2排出 之高溫高壓的冷媒氣體係朝放熱器3流入,且加熱流動於 15水流路9的水。然後,經加熱的水係經過熱水供應迴路13 ^ 而從熱水供應末端12流出。另一方面,於放熱器3冷卻之 冷媒係藉減壓部4減壓並流入吸熱器5,於此,吸收大氣 熱、太陽能等自然能量的熱能而蒸發氣化,並返回壓縮機 2。因此,一旦檢測出熱水流出,則來自壓縮機2之高溫高 20壓的冷媒氣體會立刻流入放熱器3,且加熱其中的水,而 從熱水供應末端12流出熱水。 於供應熱水時,負荷設定部18係利用與第丨實施形態 之控制部54同樣的控制方式,從熱水供應溫度與目標溫度 之偏差算出以第1算定部24算定之第i所需加熱量。即, 27 574491 進行流出熱水溫度之反饋控制。The thermal control unit 19 memorizes the relationship between the heating amount of the heat exchanger 10 and the number of revolutions of the compressor 2 in advance for each temperature. Then, the number of control revolutions is set in accordance with the air temperature so that the required heating amount set by the load setting section 18 matches the heating amount of the heat exchanger 10. Thereby, even if the temperature changes, the hot water supply control can be performed with high accuracy. The load setting unit 18 and the heating control unit 19 are configured as control units 29 corresponding to the control units 54 of the first to fourth embodiments. These control sections may be integrally formed. · In the above structure, the operation and effect will be explained. In FIG. 5, if the faucet Π is turned on, the tap water starts to flow from the water supply pipe u. It is detected by the flow detection section 20 and a signal is sent to the load setting section 18. The load setting unit 18 calculates the required heating amount, and the heating control unit 19 controls the number of revolutions of the compressor 2 based on the calculated value. Then, the high-temperature and high-pressure refrigerant gas system discharged from the compressor 2 flows into the radiator 3 and heats the water flowing through the water flow path 9. Then, the heated water system passes through the hot water supply circuit 13 ^ and flows out from the hot water supply end 12. On the other hand, the refrigerant cooled in the radiator 3 is decompressed by the decompression section 4 and flows into the heat sink 5, where it absorbs heat energy such as atmospheric heat and solar energy, evaporates and gasifies, and returns to the compressor 2. Therefore, once the outflow of hot water is detected, the high-temperature and high-pressure refrigerant gas from the compressor 2 immediately flows into the radiator 3 and heats the water therein, and the hot water flows out from the hot-water supply end 12. When supplying hot water, the load setting unit 18 uses the same control method as the control unit 54 of the first embodiment to calculate the i-th required heating calculated by the first calculation unit 24 from the deviation between the hot water supply temperature and the target temperature. the amount. That is, 27 574491 performs feedback control of the temperature of the outflow hot water.

又,亦可從流出熱水溫度與目標溫度之偏差的變化速 度來判定第1所需加熱量。若因供應熱水中之流量或給水 溫度而改變熱水供應負荷,則在流出熱水溫度與目標溫度 5 之偏差的變化速度會顯現出不同。例如,在相同的加熱量 下,流量愈多流出熱水溫度之上升則愈緩慢,而流量愈少 則愈快速。預先記憶該速度變化與所需加熱量之關係,且 從流出熱水溫度與目標溫度之偏差的變化速度來設定所需 加熱量。如此一來,較單純以溫度偏差來控制加熱量之情 10 形,可更縮短穩定地控制至所需加熱量的時間。The first required heating amount can also be determined from the rate of change of the deviation between the outflow hot water temperature and the target temperature. If the hot water supply load is changed due to the flow rate or feed water temperature in the hot water supply, the variation rate of the deviation between the outflow hot water temperature and the target temperature 5 will be different. For example, under the same heating capacity, the more the flow rate, the more slowly the hot water temperature rises, and the less the flow rate, the faster the temperature rises. The relationship between the speed change and the required heating amount is memorized in advance, and the required heating amount is set from the change rate of the deviation of the outflow hot water temperature from the target temperature. In this way, it is possible to shorten the time required for stable control to the required heating amount rather than simply controlling the heating amount based on the temperature deviation.

另一方面,以第2算定部25算定之第2所需加熱量係 算出熱水供應負荷且以該熱水供應負荷為所需加熱量。即 ,於目標溫度與給水溫度之差乘上流量檢測部20所檢測之 流量而求出熱水供應負荷,並以其為第2所需加熱量,此 15 係所謂前饋控制量。然後,以加算部26將第1所需加熱量 與第2所需加熱量相加而求出所需加熱量。藉由加上該所 需加熱量反饋控制,可將熱水供應溫度正確地控制至目標 溫度。該控制亦與第1實施形態之控制部54的控制相同。 如上所述,於本實施形態之熱水供應裝置中,熱泵循 20 環機構7係藉由冷媒流路1將壓縮機2、放熱器3、減壓部 4及吸熱器5連接成閉路。冷媒流路1係通過用以與水流 路9進行熱交換之熱交換器10。水流路9為了與熱水供應 末端12相通而構成有熱水供應迴路13。並且設有用以設 定於熱交換器10的所需加熱量之負荷設定部25及依照負 28 574491On the other hand, the second required heating amount calculated by the second calculation unit 25 is a calculation of the hot water supply load, and the hot water supply load is the required heating amount. That is, the difference between the target temperature and the feedwater temperature is multiplied by the flow rate detected by the flow rate detection unit 20 to obtain a hot water supply load, and this is the second required heating amount. This 15 is a so-called feedforward control amount. Then, the adding unit 26 adds the first required heating amount and the second required heating amount to obtain the required heating amount. By adding the required heating amount feedback control, the hot water supply temperature can be accurately controlled to the target temperature. This control is also the same as that of the control unit 54 of the first embodiment. As described above, in the hot water supply device of this embodiment, the heat pump circulation mechanism 7 is connected to the compressor 2, the radiator 3, the pressure reducing unit 4, and the heat sink 5 through the refrigerant flow path 1 in a closed circuit. The refrigerant flow path 1 passes through a heat exchanger 10 for heat exchange with the water flow path 9. The water flow path 9 includes a hot water supply circuit 13 so as to communicate with the hot water supply terminal 12. A load setting unit 25 for setting a required heating amount in the heat exchanger 10 and a load setting unit 25 according to the negative 28 574491 are provided.

荷設定部25之設定值來控制熱交換器10的加熱量之加熱 控制部19。以負荷設定部25所設定之所需加熱量為包含 熱水供應負荷或熱反應延遲等之於熱交換器之必要的熱交 換熱量。而且,由於加熱控制部19係依照該所需加熱量來 5 控制熱交換器之加熱量,故可進行沒有過多或不足之情形 的熱水供應控制。The heating control unit 19 controls the heating amount of the heat exchanger 10 by the setting value of the load setting unit 25. The required heating amount set by the load setting unit 25 is a necessary heat exchange amount including a hot water supply load or a thermal reaction delay, which is necessary for the heat exchanger. Further, since the heating control unit 19 controls the heating amount of the heat exchanger in accordance with the required heating amount, it is possible to perform hot water supply control without excessive or insufficient conditions.

又,本實施形態之熱水供應裝置係具有用以檢測熱水 供應迴路的流量之流量檢測部20。負荷設定部18係以流 量檢測部20之檢測值為標準求出所需加熱量。由於熱水供 10 應負荷與流量成正比,故於此所推定之所需加熱量係與熱 水供應負荷有關。因此,即使熱水供應負荷因流量變化而 急遽改變,亦可依照熱水供應負荷之變化而快速地進行相 對應之加熱控制。The hot water supply device of this embodiment includes a flow rate detection unit 20 for detecting the flow rate of the hot water supply circuit. The load setting unit 18 calculates the required heating amount based on the detection value of the flow detection unit 20 as a standard. Since the hot water supply load is directly proportional to the flow rate, the estimated heating amount required here is related to the hot water supply load. Therefore, even if the hot-water supply load changes abruptly due to a change in the flow rate, the corresponding heating control can be performed quickly in accordance with the change in the hot-water supply load.

又,本實施形態之熱水供應裝置係具有用以檢測給水 15 管的給水溫度之水溫檢測部21,而負荷設定部18係以水 溫檢測部21之檢測值為標準求出所需加熱量。由於熱水供 應負荷與給水溫度和目標溫度之差成正比,故若給水温度 下降則所需加熱量會增加,而給水溫度上升則所需加熱量 會減少。因此,若可藉由該給水溫度來推定所需加熱量而 20 進行熱交換器之加熱控制,則即使給水溫度變動,亦可將 伴隨該變動之流出熱水溫度變化抑制至最低限度。 又,本實施形態之熱水供應裝置係具有用以設定熱水 供應的目標溫度之溫度設定部23。因由溫度設定部23來 設定前述目標溫度,故可設定符合使用者所希望之熱水溫 29 574491 •xV.V納齡傲:微:::料-¾¾:夠::辦^玖、發明說明 S:纖::;激總錄碰激·嫩纖:纖猫 'N# 、:察Ϊ:縫隨:謂蠻義纖· 度之正確的熱水供應負荷作為所需加熱量。In addition, the hot water supply device of this embodiment includes a water temperature detection unit 21 for detecting the water supply temperature of the 15 water supply pipes, and the load setting unit 18 determines the required heating based on the detection value of the water temperature detection unit 21 the amount. Since the hot water supply load is directly proportional to the difference between the feed water temperature and the target temperature, if the feed water temperature decreases, the amount of heating required will increase, and if the feed water temperature increases, the required heating amount will decrease. Therefore, if the required heating amount can be estimated based on the feed water temperature and the heating control of the heat exchanger can be performed, even if the feed water temperature fluctuates, the temperature change of the outflow hot water accompanying the change can be suppressed to a minimum. The hot water supply device of this embodiment includes a temperature setting unit 23 for setting a target temperature for hot water supply. Since the target temperature is set by the temperature setting unit 23, a hot water temperature 29 574491 • xV.V that meets the user's expectations can be set: micro ::: 料 -¾¾: Enough :: 办 ^ 玖, description of the invention S: Fiber ::; Total recording of bumps and tender fibers: Fiber cat 'N # 、: ΪΪ: Sewing: The right hot water supply load of the right fiber is used as the required heating amount.

又,本實施形態之熱水供應裝置係具有用以檢測水流 路的流出熱水溫度之熱水溫度檢測部22,而負荷設定部18 係從熱水溫度檢測部22所檢測之流出熱水溫度與目標溫度 5 之偏差算出所需加熱量。於此所算定之所需加熱量係從偏 差之變化速度來判定熱水供應負荷。若因供應熱水中之流 量或給水溫度而改變熱水供應負荷,則在流出熱水溫度與 目標溫度之偏差的變化速度會顯現出不同。例如,在相同 的加熱量下,流量愈多流出熱水溫度之上升則愈緩慢,而 10 流量愈少則愈快速。由於抓住該速度變化,而設定所需加 熱量,故較單純以溫度偏差來控制加熱量之情形,可更縮 短穩定地控制至所需加熱量的時間。 又,本實施形態之熱水供應裝置更具有用以檢測給水 管的給水溫度之水溫檢測部21及用以檢測熱水供應迴路 15 13的流量之流量檢測部20。然後,負荷設定部18係從熱The hot water supply device of this embodiment includes a hot water temperature detection unit 22 for detecting the temperature of the hot water flowing out of the water flow path, and the load setting unit 18 is the temperature of the hot water flowing out from the hot water temperature detecting unit 22 The deviation from the target temperature of 5 calculates the required heating amount. The required heating amount calculated here is to determine the hot water supply load from the speed of deviation. If the hot water supply load is changed due to the amount of hot water supply or the feed water temperature, the speed of the deviation between the outflow hot water temperature and the target temperature will be different. For example, under the same heating capacity, the more the flow rate, the more slowly the temperature of the hot water rises, and the less the flow rate, the faster the temperature rises. Because the speed change is caught and the required heating amount is set, it is possible to shorten the time to stably control to the required heating amount rather than simply controlling the heating amount based on the temperature deviation. The hot water supply device of this embodiment further includes a water temperature detection unit 21 for detecting the water supply temperature of the water supply pipe, and a flow detection unit 20 for detecting the flow rate of the hot water supply circuit 15-13. Then, the load setting unit 18

水溫度檢測部22的檢測值與目標溫度之偏差算出與反饋控 制相關之第1所需加熱量。又,從水溫檢測部21與流量檢 測部20之檢測值與目標溫度之值算出與前饋控制相關之第 2所需加熱量。然後,將第1所需加熱量與第2所需加熱量 20 相加。藉此,由於藉由前饋控制而很快地設定目標熱量, 且藉由反饋控制來修正目標熱量與現狀,故可進行穩定且 快速之控制。 又,於本實施形態之熱水供應裝置中,加熱控制部19 係可控制壓縮機2之轉數。即,預先設定轉數與在熱交換 30 574491 玖、發明說明 . :、 —、、一 一—一 一 —、、丄…、心…5二㈣ 器10之加熱量的關係,且控制轉數以達成所設定之所需加 熱篁。藉此’可控制在可於短時間内得到所需加熱量之轉 數。 又,本實施形態之熱水供應裝置係具有用以檢測氣溫 5之氣溫檢測部28。而且,加熱控制部19係依照氣溫檢測 部28之檢測值來變更負荷設定部18之設定值且控制熱交 換器10之加熱量。如此一來,修正因氣溫變化而產生之熱 交換器10之加熱量的誤差。由於熱泵循環機構7利用大氣 鲁 熱且由吸熱器5來吸熱,故於熱交換器1〇之加熱量會對氣 10溫帶來很大的影響。因此,例如,當控制壓縮機2之轉數 時,即使是同一轉數,加熱量亦會因氣溫而改變。藉由控 制熱交換器10之加熱量以抵銷因該氣溫而產生之影響,可 進行正確的熱水供應控制。 於本實施形態中係於加算部26將第1所需加熱量與第 15 2所需加熱量相加而求出所需加熱量。但,亦可就以第t 所需加熱量為所需加熱量,且亦可就以第2所需加熱量為 · 所需加熱量。又’亦可不將其相加,而依照熱水供應時間 或流出熱水溫度來變換,且亦可於第丨所需加熱量與第2 所而加熱量分別乘上係數且相加。再者,亦可變換單獨利 20用第1所需加熱量和第2所需加熱量之情形與將其相加之 情形。如上所述,因改變第i所需加熱量與第2所需加熱 量之相加的組合或相加條件而有不同的熱水供應條件,藉 此可更提高控制之穩定性與反應性。 又,於本實施形態中,係在第2算定部25中,於目標 31 574491 凝瓣毅薄憩織:黎凝纖黎驗辟强濟;纖纖i:珍黎?^總:觸輝礙§:;:S觸热S雜 Ί、务; ϊ ϊ ί、 λ'、·· λ W、、'、、、々w > w、X ;义、ν^ϋ' r、辦日日给日日 、ί;又刀饥^3 溫度與給水溫度之偏差乘上流量而求出熱水供應負荷,並 以所演算之熱水供應負荷作為第2所需加熱量。但,若僅 欲進行概略的熱水供應負荷設定,則亦可利用於流量乘上 預定常數之推定值。此時,雖然熱水供應負荷之計算精度 5 會變差,但由於不需要水溫檢測部21與溫度設定部23, 故可使成本降低。The deviation between the detected value of the water temperature detecting unit 22 and the target temperature calculates a first required heating amount related to the feedback control. A second required heating amount related to the feedforward control is calculated from the values detected by the water temperature detection unit 21 and the flow rate detection unit 20 and the target temperature. Then, the first required heating amount and the second required heating amount 20 are added. Thereby, since the target heat is set quickly by feedforward control, and the target heat and current status are corrected by feedback control, stable and rapid control can be performed. In the hot water supply device of this embodiment, the heating control unit 19 is capable of controlling the number of revolutions of the compressor 2. That is, the relationship between the number of revolutions in advance and the heat exchange 30 574491 玖, description of the invention::, — ,, one one — one one —,,…, heart… 5 two heating device 10, and control the number of rotations In order to achieve the required heating 篁 set. By this', it is possible to control the number of revolutions which can obtain the required heating amount in a short time. The hot water supply device of this embodiment includes an air temperature detecting unit 28 for detecting the air temperature 5. The heating control unit 19 changes the setting value of the load setting unit 18 and controls the heating amount of the heat exchanger 10 in accordance with the detection value of the air temperature detecting unit 28. In this way, an error in the heating amount of the heat exchanger 10 due to a change in air temperature is corrected. Since the heat pump circulation mechanism 7 utilizes atmospheric heat and absorbs heat by the heat absorber 5, the heating amount in the heat exchanger 10 will have a great effect on the temperature of the gas 10. Therefore, for example, when the number of revolutions of the compressor 2 is controlled, even if the number of revolutions is the same, the heating amount is changed by the temperature. By controlling the heating amount of the heat exchanger 10 to offset the influence caused by the air temperature, accurate hot water supply control can be performed. In the present embodiment, the adding unit 26 adds the first required heating amount and the 152nd required heating amount to obtain the required heating amount. However, the required heating amount at the t-th may be used as the required heating amount, and the second required heating amount may be used as the required heating amount. It is also not necessary to add them, but to change them according to the hot water supply time or the temperature of the hot water flowing out, and it is also possible to multiply the coefficients of the heating required at the first and second heating and add them. Furthermore, the case where the first required heating amount and the second required heating amount are used separately and the case where they are added can be changed. As described above, there are different hot water supply conditions due to changing the combination or addition conditions of the sum of the i-th required heating amount and the second required amount of heating, thereby further improving the stability and reactivity of the control. Also, in this embodiment, it is in the second calculation section 25, and at the target 31 574491 Ning Fang Yi Zhi Ji weaving: Li Ningxian Li Li Jianqiang Ji; Fiber Xi: Zhen Li? ^ Total: Touching obstacles § :;: S touch hot S miscellaneous, business; ϊ ϊ ί, λ ', ... λ W ,,' ,,, 々w > w, X; righteousness, ν ^ ϋ 'r, day to day Day, liter, and hunger ^ 3 The difference between the temperature and the feedwater temperature is multiplied by the flow rate to obtain the hot water supply load, and the calculated hot water supply load is used as the second required heating amount. However, if only a simple hot water supply load setting is to be performed, it can also be used to estimate the flow rate multiplied by a predetermined constant. At this time, although the calculation accuracy 5 of the hot water supply load may deteriorate, since the water temperature detecting section 21 and the temperature setting section 23 are not required, the cost can be reduced.

再者,亦可利用於給水溫度與假設的目標溫度之差乘 上預定常數之推定值來進行第2算定部25中之熱水供應負 荷的演算。此時雖然熱水供應負荷之計算精度亦會變差, 10 但由於不需要流量檢測部20與溫度設定部23故可低成本 化。但,用以檢測熱水開始供應之流量開關則是必要的。 (第6實施形態)Furthermore, the calculation of the hot water supply load in the second calculation unit 25 may be performed by multiplying the difference between the feed water temperature and the assumed target temperature by an estimated value of a predetermined constant. At this time, although the calculation accuracy of the hot-water supply load may also deteriorate, 10 the cost can be reduced because the flow detection unit 20 and the temperature setting unit 23 are not required. However, a flow switch to detect the start of hot water supply is necessary. (Sixth embodiment)

第6圖係本發明第6實施形態之熱泵式熱水供應裝置 的構成圖。第6圖中,與第5實施形態之構成不同之處為 15 負荷設定部18之構造。即,具有用以設定符合熱泵循環機 構7或熱交換器10之熱反應延遲的熱量之升高設定部30 ,且於設定所需加熱量時,以加算部26加算升高設定部 30之設定值。當從熱泵循環機構7冷卻之狀態開始供應熱 水時,壓縮機2或放熱器3之溫度會上升,又,吸熱器5 20 之溫度會下降,且至變成本來正常的運轉狀態為止,需要 除了熱水供應負荷以外的熱量。所謂符合熱泵循環機構7 或熱交換器10之前述熱反應延遲的熱量則意指該熱量。 該熱量係於熱泵循環機構7或熱交換器10運轉前之溫 度與正常運轉時之溫度差乘上熱容量而求得。但,正常運 32 574491 *發明說明 si , s : BSI_Fig. 6 is a configuration diagram of a heat pump type hot water supply device according to a sixth embodiment of the present invention. In Fig. 6, the difference from the structure of the fifth embodiment is the structure of the 15 load setting unit 18. That is, there is an elevation setting section 30 for setting the amount of heat in accordance with the thermal response delay of the heat pump cycle mechanism 7 or the heat exchanger 10, and when setting the required heating amount, the setting of the elevation setting section 30 is added by the addition section 26 value. When hot water is supplied from the state in which the heat pump circulation mechanism 7 is cooled, the temperature of the compressor 2 or the radiator 3 will rise, and the temperature of the heat sink 5 20 will decrease. Heat outside the hot water supply load. The heat amount corresponding to the aforementioned thermal reaction delay of the heat pump circulation mechanism 7 or the heat exchanger 10 means the heat amount. This heat is obtained by multiplying the temperature difference between the temperature of the heat pump circulation mechanism 7 or the heat exchanger 10 before operation and the temperature during normal operation by the heat capacity. However, normal operation 32 574491 * Invention description si, s: BSI_

轉時之溫度差會因部位而有很大的不同。因此,於第6實 施形態中,係採用運轉前之溫度檢測部22所檢測之溫度與 溫度設定部23之設定值的溫度差為代表值,且於其乘上係 數而求得。但,由於以升高設定部30所求出之熱量為溫度 5 升高所需之總熱量,故為了控制壓縮機2必須變換成每單 位時間之熱量。因此,於加算部26中首先係將以第2算定 部25算定之熱水供應負荷與升高設定部30之設定熱量相 加。接著,-使該相加熱量除以壓縮機2之最大轉數時之最 大加熱量,而求出該最大加熱量之運轉時間。然後,將該 10 時間内之所需加熱量設為壓縮機2之最大加熱量。一旦超 過該運轉時間,則結束升高設定部30之設定值的相加,並 回到如第5實施形態之運轉狀態。The temperature difference during rotation will vary greatly depending on the location. Therefore, in the sixth embodiment, the temperature difference between the temperature detected by the temperature detection unit 22 before the operation and the value set by the temperature setting unit 23 is used as a representative value, and the coefficient is obtained by multiplying the factor by a factor. However, since the amount of heat obtained by the raising setting unit 30 is the total amount of heat required for raising the temperature 5, the compressor 2 must be converted into heat per unit time in order to control the compressor 2. Therefore, the adding unit 26 first adds the hot water supply load calculated by the second calculating unit 25 and the set heat of the raising setting unit 30. Next, the phase heating amount is divided by the maximum heating amount at the maximum number of revolutions of the compressor 2 to obtain the operating time of the maximum heating amount. Then, the required heating amount in this 10-time period is set as the maximum heating amount of the compressor 2. When the operation time has passed, the addition of the set values by the raising setting unit 30 is ended, and the operation returns to the operation state as in the fifth embodiment.

如上所述,於第6實施形態中,將開始熱水供應運轉 時之熱泵循環機構7或熱交換器10之熱反應延遲部分的熱 15 量加在熱水供應負荷上,且以壓縮機2之最大加熱量來加 熱熱反應延遲部分的熱量。即,本實施形態之熱水供應裝 置係負荷設定部18包含有用以設定符合熱泵循環機構7或 熱交換器10之熱反應延遲的熱量之升高設定部30。而且 ,於設定所需加熱量時加上升高設定部3 0之設定值。因此 20 ,可於開始供應熱水時或熱水供應負荷變更時進行業已加 上熱反應延遲部分之加熱控制,並可將熱反應延遲抑制至 最低限度。 又,於運轉前之熱水溫度檢測部22所檢測之溫度與溫 度設定部23之設定值的溫度差乘上係數而求出熱反應延遲 33 574491 纖凝錄纖资纖攀擊鐵務釋戀_媒_凝_賴纖纖纖$ 久、發明說明 據顯纖毅纖灘纖»麵驗纖鐵纖務As described above, in the sixth embodiment, the amount of heat 15 of the heat reaction delay portion of the heat pump circulation mechanism 7 or the heat exchanger 10 at the start of the hot water supply operation is added to the hot water supply load, and the compressor 2 The maximum amount of heating to heat the heat reaction delay part. That is, the hot water supply device system load setting unit 18 according to the present embodiment includes an increase setting unit 30 for setting the amount of heat in accordance with the thermal response delay of the heat pump cycle mechanism 7 or the heat exchanger 10. In addition, when setting the required heating amount, the setting value of the raising setting part 30 is added. Therefore, it is possible to perform the heating control which has been added with the thermal reaction delay portion at the beginning of hot water supply or when the hot water supply load is changed, and the thermal reaction delay can be suppressed to a minimum. In addition, the temperature difference between the temperature detected by the hot water temperature detection unit 22 and the set value of the temperature setting unit 23 before the operation is multiplied by a coefficient to obtain a thermal response delay 33 574491 _MEDIA_Condensing_Lai Fiber Fiber Fiber

部分的熱量。因而,無須特別準備檢測部,而可以低成本 實現該控制。 又,於第6實施形態中,係於運轉前之熱水溫度檢測 部22所檢測之溫度與溫度設定部23之設定值的溫度差乘 5 上係數而求出熱反應延遲部分的熱量。但,亦可利用熱交 換器10或壓縮機2、吸熱器5、冷媒流路1之壓縮機2的 排出部等之溫度。Part of the heat. Therefore, it is not necessary to prepare a detection section, and the control can be realized at low cost. In the sixth embodiment, the heat difference between the temperature detected by the hot water temperature detection unit 22 and the value set by the temperature setting unit 23 before the operation is multiplied by a factor of 5 to determine the heat of the thermal reaction delay portion. However, it is also possible to use the temperature of the heat exchanger 10, the compressor 2, the heat sink 5, the discharge portion of the compressor 2 of the refrigerant flow path 1, and the like.

(第7實施形態) 第7圖係本發明第7實施形態之熱泵式熱水供應裝置 10 的構成圖。第7圖中,與第5實施形態之構成不同之處為 加熱控制部19不只控制壓縮機2,亦控制減壓部4之冷媒 流路阻力及吸熱器5之吸熱量。(Seventh Embodiment) Fig. 7 is a configuration diagram of a heat pump hot water supply device 10 according to a seventh embodiment of the present invention. In Fig. 7, the difference from the fifth embodiment is that the heating control unit 19 controls not only the compressor 2 but also the refrigerant flow path resistance of the decompression unit 4 and the heat absorption amount of the heat sink 5.

減壓部4係由限流器(未圖示)及用以驅動該限流器之 步進馬達(未圖示)所構成,且藉由驅動限流器來變更冷媒 15 流路阻力。然後,加熱控制部19係預先設定減壓部4之冷 媒流路阻力與在加熱交換器10之加熱量的關係,且控制冷 媒流路阻力以達成由負荷設定部18所設定之所需加熱量。 當必須流出高溫熱水,或者因外面空氣溫度低使加熱量不 足時等,有藉由增加冷媒流路阻力以確保熱交換器之加熱 20 量為所需加熱量的作用。 又,在平常的熱水供應使用狀態下,冷媒流路8與水 流路9之溫度差愈小,則熱泵循環機構7之效率愈好。因 此,若依照水溫檢測部21所檢測之給水溫度,且確保於熱 交換器10之所需加熱量,並控制減壓部4之冷媒流路阻力 34 574491 玖、發明說明 βιThe pressure reducing section 4 is composed of a restrictor (not shown) and a stepping motor (not shown) for driving the restrictor, and the resistance of the refrigerant 15 flow path is changed by driving the restrictor. Then, the heating control section 19 sets the relationship between the refrigerant flow path resistance of the decompression section 4 and the heating amount in the heat exchanger 10 in advance, and controls the refrigerant flow path resistance to achieve the required heating amount set by the load setting section 18 . When high-temperature hot water must be discharged, or the heating amount is insufficient due to low outside air temperature, etc., it has the effect of increasing the resistance of the refrigerant flow path to ensure that the amount of heating of the heat exchanger is the required heating amount. In addition, under normal hot water supply and use conditions, the smaller the temperature difference between the refrigerant flow path 8 and the water flow path 9, the better the efficiency of the heat pump circulation mechanism 7. Therefore, if the water temperature detected by the water temperature detecting section 21 is maintained, and the required heating amount in the heat exchanger 10 is ensured, and the refrigerant flow path resistance of the decompression section 4 is controlled 34 574491 玖, description of the invention βι

以將冷媒流路8與水流路9之溫度差減至最小,則可高效 率地運轉。By minimizing the temperature difference between the refrigerant flow path 8 and the water flow path 9, it is possible to operate efficiently.

吸熱器5之吸熱量係藉由變更風扇32之馬達的轉數且 變更朝吸熱器5之送風量來控制。加熱控制部19係預先設 5 定風扇32之風量與在熱交換器10之加熱量的關係,且控 制風扇3 2之風量以達成所設定之所需加熱量。當於熱水供 應負荷極小且熱交換器10之所需加熱量過小而且壓縮機2 之轉數控制中無法再縮小時等,則減少風扇32之風量。藉 此,減少熱交換器10之加熱量且控制至所需加熱量。又, 10 當即使用壓縮機2之最大轉數加熱量亦不足時,則增加風 扇32之風量且增加熱交換器10之加熱量以控制至所需加 熱量。 如上所述,本實施形態之熱水供應裝置係加熱控制部 19可控制減壓部4之冷媒流路阻力。即,預先設定減壓部 15 4之冷媒流路阻力與在熱交換器10之加熱量的關係,且控The amount of heat absorbed by the heat sink 5 is controlled by changing the number of rotations of the motor of the fan 32 and changing the amount of air supplied to the heat sink 5. The heating control unit 19 sets the relationship between the air volume of the fan 32 and the heat amount in the heat exchanger 10 in advance, and controls the air volume of the fan 32 to achieve the set required heating amount. When the hot water supply load is extremely small, the required heating amount of the heat exchanger 10 is too small, and the rotation speed of the compressor 2 cannot be reduced any more, the air volume of the fan 32 is reduced. Thereby, the heating amount of the heat exchanger 10 is reduced and controlled to a required heating amount. In addition, when the maximum heating capacity of the compressor 2 is insufficient, the air volume of the fan 32 is increased and the heating capacity of the heat exchanger 10 is increased to control the required heating capacity. As described above, the hot water supply device of this embodiment is the heating control unit 19 that can control the refrigerant flow path resistance of the decompression unit 4. That is, the relationship between the refrigerant flow path resistance of the decompression section 15 4 and the heating amount in the heat exchanger 10 is set in advance, and

制冷媒流路阻力以達成所設定之所需加熱量。因此,當必 須流出高溫熱水,或者因外面空氣溫度低使加熱量不足時 等,藉由增加冷媒流路阻力,可確保熱交換器之加熱量為 所需加熱量。又,依照水溫檢測部21之檢測溫度來進行減 20 壓部4之冷媒流路阻力的控制。即,預先設定符合給水溫 度之減壓部4的冷媒流路阻力與在熱交換器10之加熱量的 關係,且控制冷媒流路阻力以達成所設定之所需加熱量。 當必須流出高溫熱水,或者因外面空氣溫度低使加熱量不 足時等,藉由增加冷媒流路阻力,可確保熱交換器1 〇之加 35 574491Refrigerant flow path resistance to achieve the required heating amount set. Therefore, when high-temperature hot water must be discharged, or the heating capacity is insufficient due to low outside air temperature, etc., by increasing the resistance of the refrigerant flow path, the heating capacity of the heat exchanger can be ensured. In addition, the refrigerant flow path resistance of the pressure reducing section 4 is controlled in accordance with the temperature detected by the water temperature detecting section 21. That is, the relationship between the resistance of the refrigerant flow path and the heating amount in the heat exchanger 10 in the decompression section 4 according to the feed water temperature is set in advance, and the resistance of the refrigerant flow path is controlled to achieve the set required heating amount. When high-temperature hot water must be discharged, or the amount of heating is insufficient due to low outside air temperature, etc., by increasing the resistance of the refrigerant flow path, the heat exchanger 1 〇 plus 35 574491 can be ensured.

熱量為所需加熱量。又,於平常供應熱水時,亦可藉由給 水溫度而控制成加熱效率最佳之冷媒流路阻力。 又,本實施形態之熱水供應裝置係加熱控制部19可控 制吸熱器5之吸熱量。因此,藉由風扇32之風量來控制吸 5 熱器5從大氣熱吸取之吸熱量。然後,預先設定風扇32之 風量與在熱交換器10之加熱量的關係,且控制風扇32之 風量以達成所設定之所需加熱量。當於熱水供應負荷極小 且熱交換器10之所需加熱量過小而且壓縮機2之轉數控制 · 中無法再縮小時等,則減少風扇32之風量,藉此可減少熱 10 交換器10之加熱量且控制至所需加熱量。 (苐8實施形態) 第8圖係本發明第8實施形態之熱泵式熱水供應裝置 的構成圖。第8圖中,與第5實施形態之構成不同之處為 從熱交換器10之水流路9的中央部分出分歧管33,且與 15設於熱水供應迴路13之混合閥34相連接,而變更熱交換 器1〇之傳熱條件。於該構造中,加熱控制部19係藉由控 β 制混合閥34之開啟度,來控制從水流路9之分歧管33流 動於下游之水量。然後,藉由控制水流路9之流量或流速 ,且改變冷媒流路8與水流路9之傳熱條件,來控制在熱 2〇父換器10之加熱量。若水量降低,則水流路9内之熱傳導 率會下降,結果,加熱量會下降。然後,若不從水流路9 之分歧管33流動於下游,則肖無法進行熱交換,且傳熱面 積約變為-半者有同樣的作用。如此一來,若改變水流路 長度或水畺則加熱昼會成正比地改變。由於若改變該 36 574491 歲 '蠢明說明、、、…: 、 等條件則加熱量會立刻改變,故可進行提高熱反應性之控 制’亦可應付所需加熱量急遽改變之情況。 如此一來,於本實施形態之熱水供應裝置中,加熱控 制部19係變更熱交換器10之水流路9的流速或熱量等傳 5 熱條件來控制加熱量。具體而言,係變更熱交換器10之水 流路的長度或水量。由於熱交換器10之加熱量與傳熱面積 或熱傳導率成正比,故若改變水流路之長度或水量則可成 正比地政變加熱量。由於若改變該等條件則加熱量會立刻 · 改變’故可進行提高熱反應性之控制。 0 又’雖然於第8實施形態中係從熱交換器1〇之中央部 分出分歧管33,但亦可於熱交換器1〇之上游分歧而與熱 交換器10並聯,以變更流動於熱交換器1〇整體之流量。 又’從熱交換器10之上游側或下游側分歧皆可得到同樣的 效果。 5 又,亦可包含第5至第8實施形態所述之負荷設定部 18與加熱控制部19而構成第1至第4實施形態之控制部 · 54。,若構成如上,則可進行更為細腻之熱水供應溫度控 制,並提高對熱水供應負荷之隨動性。 (第9實施形態) > 第9圖係本發明第9實施形態之熱泵式熱水供應裝置 的構成圖。如第9圖所示’本實施形態係將三台壓縮機2Α 、2Β、2C並列地設置於熱泵循環機構7,且控制部54係 控制壓縮機2A、2B、2C之台數與轉數。於本實施形態中 ,係控制壓縮機2A之轉數,且進行微妙之加熱能力控制 37 574491The heat is the amount of heating required. In addition, when hot water is normally supplied, the resistance to the refrigerant flow path with the best heating efficiency can be controlled by the water temperature. The hot water supply device of this embodiment is a heating control unit 19 that can control the amount of heat absorbed by the heat sink 5. Therefore, the amount of heat absorbed by the heat sink 5 from the heat of the atmosphere is controlled by the air volume of the fan 32. Then, the relationship between the air volume of the fan 32 and the heating amount in the heat exchanger 10 is set in advance, and the air volume of the fan 32 is controlled to achieve the set required heating amount. When the hot water supply load is extremely small, the required heating capacity of the heat exchanger 10 is too small, and the rotation speed of the compressor 2 cannot be reduced, etc., the air volume of the fan 32 is reduced, thereby reducing the heat 10 exchanger 10 The heating amount is controlled to the required heating amount. (Embodiment 8) Fig. 8 is a block diagram of a heat pump type hot water supply device according to an eighth embodiment of the present invention. In FIG. 8, the structure differs from the fifth embodiment in that a branch pipe 33 extends from the central portion of the water flow path 9 of the heat exchanger 10 and is connected to a mixing valve 34 provided in the hot water supply circuit 13. The heat transfer conditions of the heat exchanger 10 are changed. In this structure, the heating control unit 19 controls the opening degree of the β control mixing valve 34 to control the amount of water flowing downstream from the branch pipe 33 of the water flow path 9. Then, by controlling the flow rate or flow velocity of the water flow path 9 and changing the heat transfer conditions of the refrigerant flow path 8 and the water flow path 9, the heating amount of the heat exchanger 10 is controlled. When the amount of water decreases, the thermal conductivity in the water flow path 9 decreases, and as a result, the amount of heating decreases. Then, if it does not flow downstream from the branch pipe 33 of the water flow path 9, Xiao cannot perform heat exchange, and the heat transfer area becomes approximately -half, which has the same effect. In this way, if the length of the water flow path or the leeches is changed, the heating day will change in proportion. If the 36,574,491-year-old 'stupid explanation ,,,, ...:, etc. conditions are changed, the heating amount will be changed immediately, so it can be controlled to improve the thermal reactivity', and it can also cope with the sudden change of the required heating amount. In this way, in the hot water supply device of this embodiment, the heating control unit 19 controls the heating amount by changing the heat transfer conditions such as the flow velocity or heat of the water flow path 9 of the heat exchanger 10. Specifically, the length or amount of water in the water flow path of the heat exchanger 10 is changed. Since the heating amount of the heat exchanger 10 is directly proportional to the heat transfer area or thermal conductivity, if the length or amount of the water flow path is changed, it can be proportional to the heating amount of the land coup. If these conditions are changed, the amount of heating will be immediately changed. Therefore, control to improve thermal reactivity can be performed. In the eighth embodiment, although the branch pipe 33 is formed from the central portion of the heat exchanger 10, it can be branched upstream of the heat exchanger 10 and connected in parallel with the heat exchanger 10 to change the flow of heat. Exchanger 10 overall traffic. The same effect can be obtained by diverging from the upstream side or the downstream side of the heat exchanger 10. 5 Also, the load setting unit 18 and the heating control unit 19 described in the fifth to eighth embodiments may be included in the control unit 54 of the first to fourth embodiments. If the structure is as above, more delicate hot water supply temperature control can be performed, and the follow-up of hot water supply load can be improved. (Ninth Embodiment) > Fig. 9 is a configuration diagram of a heat pump type hot water supply device according to a ninth embodiment of the present invention. As shown in Fig. 9 ', this embodiment is a system in which three compressors 2A, 2B, and 2C are arranged in parallel to the heat pump cycle mechanism 7, and a control unit 54 controls the number and revolutions of the compressors 2A, 2B, and 2C. In this embodiment, the rotation speed of the compressor 2A is controlled, and delicate heating capacity control is performed. 37 574491

从、%、V!s、、、、、、'<:'、❖、认、'、V、、、、0、、、\、、、SNNS s s、'、s、s、、·ΛΛ、ΥΛ、方今、w 5 \ d 、、、、、、、^、Ί、Ά》Ά、、 、>、、、\》'、、'、'彳、、:夂、、、)、、、、、、、Λ、、、、、、'、仏、ρ 故相乂故界热'松:^5¾^¾汾傲6¾¾¾¾¾¾ 纖纖凝纖麵臟藤灘麵務擺麵 ,而壓縮機2B、2C則進行開關控制。當在淋浴或泡澡之 裝滿熱水等熱水供應負荷需要強大能力時,係運轉兩台或 三台壓縮機。當夏天在廚房清洗餐具等熱水供應負荷極少 時,則藉由單獨運轉壓縮機2A,來應付廣泛的熱水供應負 5 荷變化。From,%, V! S ,,,,,, '<:', ❖, Recognition, ', V ,,,, 0 ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, SNSN ss,', s, s,, ΛΛ , ΥΛ, 方今, w 5 \ d ,,,,,,, ^, Ί, Ά》 Ά ,,, > ,, \》 ',,', '彳 ,,: 夂 ,,,), ,,,,,, Λ ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, loose, ^ 5¾ ^ ¾fen proud 6¾¾¾¾¾¾ , 2C is for switch control. When a hot water supply load, such as filling hot water in a shower or bath, requires strong capacity, two or three compressors are operated. When the load of hot water supply such as washing dishes in the kitchen is very small in summer, the compressor can be operated by 2A alone to cope with a wide range of changes in hot water supply load.

如上所述,本實施形態之熱水供應裝置係於熱泵循環 機構7備有多數壓縮機2A、2B、2C,且控制部54係控制 壓縮機之台數。當使用在熱水供應負荷會大幅改變時,一 台壓縮機在控制幅度方面有其限度,而無法進行滿意的熱 10 水供應控制。但,如上所述,於控制壓縮機的台數之方法 中,若依照熱水供應負荷來改變台數,則可應付廣泛的熱 水供應負荷變化。As described above, the hot water supply device of this embodiment is provided with a plurality of compressors 2A, 2B, and 2C in the heat pump circulation mechanism 7, and the control unit 54 controls the number of compressors. When the load on hot water supply will change drastically, a compressor has its limits in terms of control range, and it cannot perform satisfactory hot water supply control. However, as described above, in the method of controlling the number of compressors, if the number of units is changed in accordance with the hot water supply load, it is possible to cope with a wide range of changes in the hot water supply load.

又,壓縮機之台數為兩台亦可,且即使是三台以上亦 可得到同樣的效果。又,亦可控制所有多台壓縮機之轉數 15 ,且順利地控制台數變換。再者,亦可使壓縮機排成一列 地連接,並控制排出壓力。 (第10實施形態) 第10圖係本發明第10實施形態之熱泵式熱水供應裝 置的構成圖。如第10圖所示,本實施形態之熱泵式熱水供 20 應裝置係具有兩台熱泵循環機構。用以構成第1個熱泵循 環機構之第1單元92D係收納有包含風扇32D之吸熱器 5D、壓縮機2D、減壓部4D及驅動部93D,且配置於屋外 作為室外機器。用以構成第2個熱泵循環機構之第2單元 92E係收納有包含風扇32E之吸熱器5E、壓縮機2E、減 38 574491In addition, the number of compressors may be two, and the same effect can be obtained even with three or more compressors. In addition, the number of revolutions of all multiple compressors can be controlled, and the number of control units can be changed smoothly. Furthermore, the compressors can be connected in a row and the discharge pressure can be controlled. (Tenth embodiment) Fig. 10 is a configuration diagram of a heat pump-type hot water supply device according to a tenth embodiment of the present invention. As shown in Fig. 10, the heat pump hot water supply device of this embodiment has two heat pump circulation mechanisms. The first unit 92D, which constitutes the first heat pump circulation mechanism, contains a heat sink 5D including a fan 32D, a compressor 2D, a pressure reducing section 4D, and a driving section 93D, and is arranged outdoors as an outdoor device. The second unit, 92E, which constitutes the second heat pump circulation mechanism, contains a heat sink 5E including a fan 32E, a compressor 2E, and a minus 38 574491.

壓部4E及驅動部93E,且同樣地配置於屋外作為室外機器 。然後,於第3單元86係收納有與給水管11和流出熱水 配管13相連接之熱交換器87且配置於屋内。The pressing portion 4E and the driving portion 93E are similarly arranged outdoors as outdoor equipment. A heat exchanger 87 connected to the water supply pipe 11 and the outflow hot water pipe 13 is housed in the third unit 86 and is arranged in the room.

熱交換器87係於水流路9之上游側與下游側具有放熱 5 器88與放熱器89兩個放熱器,且兩放熱器係分別加熱水 流路9之流水。然後,冷媒流路90D與冷媒流路91D係使 第1單元92D與第3單元86之放熱器88相連接。又,冷 媒流路90E與冷媒流路91E係使第2單元92E與第3單元 86之放熱器89相連接。然後,控制部94係依照所算出之 10 熱水供應負荷,而將運轉指示輸出至驅動部93D與驅動部 93E以進行熱水供應控制。依照此時的熱水供應負荷,而 停止第2單元92E,並藉由控制壓縮機2D與壓縮機2E之 轉數來實現目標溫度之熱水供應。控制部94與驅動部93D 或驅動部93E之組合係相當於第1至第4實施形態之控制 15 部54或第5至第8實施形態之控制部29。於前述任何一 者包含第5至第8實施形態之負荷設定部18與加熱控制部 19而構成亦可。 於以上之構造中,由於藉由增減所構成之熱果的台數 來改變最大熱水供應能力,故可藉由台數而簡單地調整因 20 家庭人數的不同等而相異之所需熱水供應能力。又,由於 將兩個熱泵循環機構分成三個單元來配置,故可分散重量 ,且搬運或施工會較容易。 又,當使用在熱水供應負荷會大幅改變時,如上所述 ,一台習知構造之熱泵循環機構在控制幅度方面有其限度 39 574491 發明說明 ,而無法進行滿意的熱水供應控制。如本實施形態所述, 於設置兩個熱泵循環機構,且控制運轉台數或壓縮機之轉 數的方法中,可依照熱水供應負荷來進行廣泛的熱水供應 能力變更。又,於開始運轉時,藉由充分運轉兩個熱泵循 5 環機構,使熱水溫度之升高速度變快。 再者,由於當熱水供應負荷少時可停止一台熱泵循環 機構,故即使於低負荷時,亦可進行高效率運轉。The heat exchanger 87 is provided on the upstream side and the downstream side of the water flow path 9 with two heat radiators 88 and 89, and the two heat radiators respectively heat the water flowing in the water flow path 9. The refrigerant flow path 90D and the refrigerant flow path 91D connect the first unit 92D and the radiator 88 of the third unit 86. The refrigerant flow path 90E and the refrigerant flow path 91E connect the second unit 92E and the radiator 89 of the third unit 86. Then, the control unit 94 outputs an operation instruction to the driving unit 93D and the driving unit 93E in accordance with the calculated hot water supply load to perform hot water supply control. The second unit 92E is stopped in accordance with the hot water supply load at this time, and the hot water supply at the target temperature is achieved by controlling the number of revolutions of the compressor 2D and the compressor 2E. The combination of the control section 94 and the driving section 93D or the driving section 93E corresponds to the control section 15 of the first to fourth embodiments 54 or the control section 29 of the fifth to eighth embodiments. Any of the foregoing may include a load setting unit 18 and a heating control unit 19 according to the fifth to eighth embodiments. In the above structure, since the maximum hot water supply capacity is changed by increasing or decreasing the number of hot fruit constituted, the number of units can be easily adjusted according to the needs of 20 families. Hot water supply capacity. In addition, since the two heat pump circulation mechanisms are divided into three units to be arranged, the weight can be dispersed, and handling or construction can be easier. In addition, when the load for hot water supply is greatly changed, as described above, a conventionally constructed heat pump cycle mechanism has a limit in terms of control range 39 574491 Invention Description, and it is impossible to perform satisfactory hot water supply control. As described in this embodiment, in the method of providing two heat pump circulation mechanisms and controlling the number of operation units or the number of compressor revolutions, a wide range of hot water supply capacity can be changed in accordance with the hot water supply load. In addition, at the start of the operation, the temperature of the hot water is increased faster by fully operating the two heat pump five-loop mechanism. Furthermore, since a heat pump circulation mechanism can be stopped when the hot water supply load is small, high-efficiency operation can be performed even at a low load.

又,雖然於本實施形態中係對水流路9直列地配置熱 交換器86之放熱器88與放熱器89於上游側與下游側,但 10 亦可對水流路9並列地配置兩放熱器。此時由於可同時使 水流路9個別對放熱器之入口水溫與自來水溫度相同,故 熱交換率會提高。又,如上所述,亦可藉由配置成並列兩 個放熱器,且使水流路9對該等放熱器亦並列地分流,並 使其分別相對,而使兩放熱器之加熱量分別獨立並加以控 15 制。此時,為多數並列地設置熱交換器之構造亦可。再者 ,藉由控制該並列之水流路所合流之混合比例,亦可控制 熱水供應溫度。 又,與其他實施形態同樣地,若設置氣溫檢測部28, 且將其檢測結果輸入控制部94,並反映在驅動部93D、 20 93E之控制上,則進而可更細腻地控制熱水供應能力。 又,於本實施形態中,雖然係構造成具有兩個熱泵循 環機構,但藉由進一步增加熱栗循環機構數量,可實現強 大能力且廣泛的熱水供應能力可變性。 又,於本實施形態中,雖然係構造成將熱泵循環機構 40 574491 分割成三個單元,但即使一體地構成亦可提高熱水供應能 力0 又,如上所述,若將設置多數熱泵循環機構且控制運 轉台數或壓縮機之轉數的方法適用於第1至第9實施形態 5 ,則可進一步提高對熱水供應負荷之隨動性。 L圖式簡單說明3In the present embodiment, although the heat exchanger 88 and the heat radiator 89 of the heat exchanger 86 are arranged in parallel to the water flow path 9 on the upstream side and the downstream side, 10 the two heat radiators may be arranged in parallel to the water flow path 9. At this time, since the inlet water temperature of the water flow path 9 to the radiator can be made the same as the tap water temperature, the heat exchange rate will be increased. In addition, as described above, the two radiators can be arranged in parallel, and the water flow path 9 can also be divided in parallel with the radiators and made to face each other, so that the heating amounts of the two radiators are independent and Be controlled 15 times. In this case, a structure in which a plurality of heat exchangers are provided in parallel may be used. Furthermore, the hot water supply temperature can also be controlled by controlling the mixing ratio of the confluence of the juxtaposed water flow paths. Also, as in the other embodiments, if the air temperature detection unit 28 is provided and the detection result is input to the control unit 94 and reflected in the control of the driving units 93D and 20 93E, the hot water supply can be controlled more delicately. ability. Furthermore, in this embodiment, although it is configured to have two heat pump circulation mechanisms, by further increasing the number of heat pump circulation mechanisms, it is possible to realize a large capacity and wide variability of hot water supply capacity. Moreover, in this embodiment, although the heat pump circulation mechanism 40 574491 is divided into three units, even if it is integrated, the hot water supply capacity can be improved. As described above, if a large number of heat pump circulation mechanisms are provided Furthermore, the method of controlling the number of operating units or the number of revolutions of the compressor is applicable to the first to ninth embodiments 5 and can further improve the followability of the hot water supply load. L schema simple explanation 3

第1圖係本發明第1實施形態之熱泵式熱水供應裝置 的構成圖。 第2圖係本發明第2實施形態之熱泵式熱水供應裝置 10 的構成圖。 第3圖係本發明第3實施形態之熱泵式熱水供應裝置 的構成圖。 第4圖係本發明第4實施形態之熱泵式熱水供應裝置 的構成圖。 15 第5圖係本發明第5實施形態之熱泵式熱水供應裝置Fig. 1 is a configuration diagram of a heat pump type hot water supply device according to a first embodiment of the present invention. Fig. 2 is a configuration diagram of a heat pump hot water supply device 10 according to a second embodiment of the present invention. Fig. 3 is a configuration diagram of a heat pump type hot water supply device according to a third embodiment of the present invention. Fig. 4 is a configuration diagram of a heat pump type hot water supply device according to a fourth embodiment of the present invention. 15 FIG. 5 is a heat pump hot water supply device according to a fifth embodiment of the present invention

的構成圖。 第6圖係本發明第6實施形態之熱泵式熱水供應裝置 的構成圖。 第7圖係本發明第7實施形態之熱泵式熱水供應裝置 20 的構成圖。 第8圖係本發明第8實施形態之熱泵式熱水供應裝置 的構成圖。 第9圖係本發明第9實施形態之熱泵式熱水供應裝置 的構成圖。 41 574491 玖、發明說明 第10圖係本發明第10實施形態之熱泵式熱水供應裝 置的構成圖。 第11圖係習知之熱泵式熱水供應裝置的構成圖。 【圖式之主要元件代表符號表】 1…雜流路 22…熱水溫度檢測部 2、2D、2E...壓縮機 23…溫度設定部 3...第2放熱器 24...第1算定部 3A···第1放熱器 25…第2算定部 4、4D、4E···減壓部 26...加算部 5、5D、5E···吸熱器 27...頻率控制部 7…熱泵循環機構 28...氣ί»測部 8…雜流路 29...控制部 9…水流路 30·.·升高設定部 10…熱交換器 32、32D、32Ε···風扇 11···給水管 33···分歧管 12…熱水供應末端 34...混合閥 13…熱水供應迴路 38···加溫部 15…熱水供應配管 39"·上游部 16···蓮蓬頭 40…蓄熱部 17…水龍頭 41…儲存槽 18…負荷設定部 43·.·入口管 19...加熱控制部 44.··出口管 20...流量檢測部 45…隔熱材料 21…水溫檢測部 46···分歧部Composition diagram. Fig. 6 is a configuration diagram of a heat pump type hot water supply device according to a sixth embodiment of the present invention. Fig. 7 is a configuration diagram of a heat pump hot water supply device 20 according to a seventh embodiment of the present invention. Fig. 8 is a configuration diagram of a heat pump type hot water supply device according to an eighth embodiment of the present invention. Fig. 9 is a configuration diagram of a heat pump type hot water supply device according to a ninth embodiment of the present invention. 41 574491 发明 Description of the invention Fig. 10 is a block diagram of a heat pump-type hot water supply device according to a tenth embodiment of the present invention. Fig. 11 is a block diagram of a conventional heat pump hot water supply device. [Representative symbol table of main components of the figure] 1 ... Miscellaneous flow path 22 ... Hot water temperature detection section 2, 2D, 2E ... Compressor 23 ... Temperature setting section 3 ... Second radiator 24 ... 1 Calculation section 3A ... First heat radiator 25 ... Second calculation section 4, 4D, 4E ... Decompression section 26 ... Addition section 5, 5D, 5E ... Heat sink 27 ... Frequency control Section 7 ... Heat pump circulation mechanism 28 ... Gas measurement section 8 ... Miscellaneous flow path 29 ... Control section 9 ... Water flow path 30 .. · Elevation setting section 10 ... Heat exchanger 32, 32D, 32E ... · Fan 11 ··· Water supply pipe 33 ··· Dividing pipe 12 ... Hot water supply end 34 ... Mixing valve 13 ... Hot water supply circuit 38 ... Heating section 15 ... Hot water supply pipe 39 " Upstream section 16 ... Shower head 40 ... Heat storage unit 17 ... Faucet 41 ... Storage tank 18 ... Load setting unit 43 ... Inlet pipe 19 ... Heating control unit 44 ... Outlet pipe 20 ... Flow detection unit 45 ... Hot material 21 ... Water temperature detection section 46 ... Bifurcation section

42 57449142 574491

47···合流部 51…儲存溫度檢測部 54.. .控制部 60.. .加溫部 61···蓄熱部 62…儲存槽 63···入口管 70···加溫部 71···蓄熱部 72…儲存槽 73···入口管 80···加溫部 81…水循環路 82…儲存槽 83···入口管 86···第3單元 87…熱交換器 88、89...放熱器 92D…第1單元 92E·.·第2單元 93D、93E···驅動部 94.. .控制部 201…冷媒流路 202.. .壓縮機 203.. .放熱器 204…減壓部 205…吸熱器 207…熱泵循環機構 208…冷媒流路 209…水流路 210.. .熱交換器 211"·給水管 212…熱水供應末端 213…熱水供應迴路 214…溫度感應器 215.. .變換器47 ... Confluence unit 51 ... Storage temperature detection unit 54 ... Control unit 60 ... Heating unit 61 ... Heat storage unit 62 ... Storage tank 63 ... Inlet pipe 70 ... Heating unit 71 ... ·· Heat storage section 72 ... Storage tank 73 ··· Inlet pipe 80 ··· Heating section 81 ... Water circulation path 82 ... Storage tank 83 ··· Inlet pipe 86 ··· Third unit 87 ... Heat exchanger 88, 89 ... radiator 92D ... 1st unit 92E ... 2nd unit 93D, 93E ... drive unit 94 ... control unit 201 ... refrigerant flow path 202 ... compressor 203 ... radiator 204 ... Decompression section 205 ... heat absorber 207 ... heat pump circulation mechanism 208 ... refrigerant flow path 209 ... water flow path 210 ... heat exchanger 211 " water supply pipe 212 ... hot water supply end 213 ... hot water supply circuit 214 ... temperature sensor 215 ... converter

90D、90E、91D、91E...冷媒流路 4390D, 90E, 91D, 91E ... Refrigerant flow path 43

Claims (1)

574491574491 1. 一種熱泵式熱水供應裝置,包含有: 熱泵循環機構,具有:壓縮機、放熱器、減壓部 、吸熱器及使前述壓縮機、前述放熱器、前述減壓部 及前述吸熱器構成為閉路之冷媒流路; 熱交換器,具有用以與前述冷媒流路進行熱交換 之水流路; 給水管,用以將自來水供給至前述水流路; 熱水供應迴路,係連接成可從前述水流路通水至 熱水供應末端者;及 10 加溫部,用以加熱由前述給水管與前述水流路與 前述熱水供應迴路所構成之通路之至少一處的水。 2. 如申請專利範圍第1項之熱泵式熱水供應裝置,其中 前述加溫部係包含有與前述給水管與前述熱交換器與 前述熱水供應迴路中任一者排成一列之蓄熱部。 15 3. 如申請專利範圍第1項之熱泵式熱水供應裝置,其中 前述加溫部具有並列地連接於前述給水管與前述熱交 換器與前述熱水供應迴路中任一者之蓄熱部。 4. 如申請專利範圍第2與3項中任一項之熱泵式熱水供 應裝置,其中前述加溫部具有用以混合前述給水管與 前述熱交換器與前述熱水供應迴路中任一者之流水與 藉由前述蓄熱部加熱之水之混合部。 5·如申請專利範圍第2與3項中任一項之熱泵式熱水供 應裝置,其中前述加溫部具有用以變換前述給水管與 前述熱交換器與前述熱水供應迴路中任一者之流水與 44 20 5 10 15 20 猎由刖述蓄熱部加熱之水並使其流動之變換部。 2與3項巾任-項之減式熱水供 '裝置其中則述加溫部具有用以將蓄熱溫度保持於 預定溫度之保溫部。 7·:申請專利範圍第6項之熱泵式熱水供應裝置,其中 月’J述加溫部包含前述放熱器。 兑申π專利辜巳圍第i項之熱系式熱水供應裝置,其中 述加’皿"卩具有至少包含前述給水管與前述熱交換器 與前述熱水供應迴路之其中一個而形成之水循環路, 且保持前述水循環路之循環水的溫度。 9·如I請專利範圍第8項之熱泵式熱水供應裝置,係驅 月丨J述熱栗循%機構且藉由前述水流路來保持前述水 循環路之循環水的溫度。 申吻專利範圍第8項之熱1式熱水供應裝置,其中 前述水循環路係包含有蓄熱部。 U ·如申請專利範圍第2、3戎〗 :¾ 10項中任一項之熱泵式熱 K供應裝置’其中則述蓄熱部係以相當於因前述熱栗 循環機構與前述熱交換器之至少一者的熱反應延遲而 產生之不足的熱量為蓄熱量。 12·如申請專利範圍第2、3或1〇 水供應裝置,係使前述蓄熱部 供應迴路之熱水供應溫度高。 項中任一項之熱泵式熱 之畜熱溫度較前述熱水 13·如申請專利範圍第 水供應裝置,其中 2、3或10項中任一項之熱泵式熱 則述蓄熱部係具有用以儲存由前述 45 574491 給水管及前述熱交換器及前述熱水供應迴路所構成之 水循環路之至少一處的水之儲存槽。 ^ 一種熱泵式熱水供應裝置,包含有·· 熱系循環機構,具有:壓縮機、放熱器、減壓部 、吸熱器及使前述壓縮機、前述放熱器、前述減壓部 及前述吸熱器構成為閉路之冷媒流路;1. A heat pump type hot water supply device, comprising: a heat pump circulation mechanism including a compressor, a heat radiator, a pressure reducing section, a heat absorber, and a structure including the compressor, the heat radiator, the pressure reducing section, and the heat absorber A closed-circuit refrigerant flow path; a heat exchanger having a water flow path for heat exchange with the refrigerant flow path; a water supply pipe for supplying tap water to the water flow path; a hot water supply circuit connected to be connected from the foregoing The water flow path passes water to the end of the hot water supply; and 10 heating sections for heating water in at least one of the paths formed by the water supply pipe, the water flow path, and the hot water supply circuit. 2. The heat pump type hot water supply device according to item 1 of the patent application range, wherein the heating section includes a heat storage section aligned with any one of the water supply pipe, the heat exchanger, and the hot water supply circuit. . 15 3. The heat pump hot water supply device according to item 1 of the patent application range, wherein the heating section has a heat storage section connected in parallel to any one of the water supply pipe, the heat exchanger, and the hot water supply circuit. 4. The heat pump hot water supply device according to any one of claims 2 and 3, wherein the heating section includes any one of the water supply pipe, the heat exchanger, and the hot water supply circuit. The mixing section of the flowing water and the water heated by the heat storage section. 5. The heat pump type hot water supply device according to any one of claims 2 and 3, wherein the heating section is provided to change any one of the water supply pipe, the heat exchanger, and the hot water supply circuit. The flowing water and 44 20 5 10 15 20 hunt for the conversion part of the water heated by the thermal storage part and flowing. The items 2 and 3 include any one of the items of the reduced-type hot water supply device. The heating section includes a heat preservation section for maintaining the heat storage temperature at a predetermined temperature. 7 ·: The heat pump type hot water supply device according to item 6 of the patent application, wherein the heating section mentioned above includes the aforementioned radiator. The heat-type hot water supply device according to item i of the patent application, which is formed by including at least one of the aforementioned water supply pipe, the aforementioned heat exchanger, and the aforementioned hot water supply circuit. The water circulation path maintains the temperature of the circulating water in the water circulation path. 9. The heat pump type hot water supply device according to item 8 of the patent scope, which drives the heat pump through the mechanism described above and maintains the temperature of the circulating water in the water circulation path through the water flow path. The kiss type 1 hot water supply device of claim No. 8 in which the aforementioned water circulation system includes a heat storage section. U · If the scope of patent application is No. 2 and No. 3: ¾ The heat pump type K supply device of any one of 10 items, wherein the heat storage unit is equivalent to at least the heat pump circulation mechanism and the heat exchanger. One of the insufficient heat generated due to the delayed thermal reaction is the stored heat. 12. If the patent application covers the second, third or tenth water supply device, the hot water supply temperature of the aforementioned heat storage section supply circuit is high. The heat temperature of any of the heat pump type animals is higher than that of the aforementioned hot water. For example, if the water supply device of the scope of the patent application, the heat pump type of any of 2, 3 or 10, the heat storage unit has a useful function. A storage tank for storing water in at least one of the water circulation paths constituted by the aforementioned 45 574491 water supply pipe, the aforementioned heat exchanger, and the aforementioned hot water supply circuit. ^ A heat pump-type hot water supply device including a heat circulation mechanism including a compressor, a radiator, a decompression unit, a heat sink, and a compressor, a heat sink, a decompression unit, and a heat sink Constitute a closed-circuit refrigerant flow path; 熱父換器’具有用以與前述冷媒流路進行熱交換 之水流路; 給水管’用以將自來水供給至前述水流路; 熱水供應迴路,係連接成可從前述水流路通水至 熱水供應末端者; 負荷設定部,用以設定於前述熱交換器之加熱量 :及 加熱控制部,係依照前述負荷設定部之設定值來 控制前述熱交換器之加熱量者。The heat parent converter has a water flow path for heat exchange with the refrigerant flow path; a water supply pipe is used to supply tap water to the water flow path; a hot water supply circuit is connected to pass water from the water flow path to the heat The end of the water supply; the load setting section for setting the heating amount of the heat exchanger: and the heating control section for controlling the heating amount of the heat exchanger according to the setting value of the load setting section. 15·如申請專利範圍帛14項之熱栗式熱水供應裝置,更具 有用以檢測前述熱水供應迴路的流量之流量檢測部, 且别述負荷設定部係以前述流量檢測部之檢測值為基 準求出加熱量。 16·如申請專利範圍帛14項之熱栗式熱水供應裝置,更具 =用以檢測前述給水管的給水溫度之水溫檢測部,且 月1J述負何設定部係以前述水溫檢測部t檢測值為基準 求出加熱量。 17·如申請專利範圍帛14項之歸式熱水供應裝置,更具 46 574491 、由諸亩^Γί銘匪甲|^3專不」軺圍 、、、、、》、i· ~!igg錢 jigi| 續廳Ai麵ill15. If the hot-pump-type hot water supply device with a scope of 14 patent applications, it also has a flow detection section for detecting the flow of the hot water supply circuit, and the load setting section uses the detection value of the flow detection section. Determine the heating amount as a reference. 16 · If the patent application scope 14 items of hot chestnut-type hot water supply device, there is a water temperature detection unit for detecting the water supply temperature of the aforementioned water supply pipe, and the setting unit described in 1J is based on the aforementioned water temperature detection The heating amount was obtained based on the detected value of the portion t. 17 · If the scope of the patent application is 14 items, the return-type hot water supply device is 46 574491, which is composed of acres ^ Γί 铭 匪 甲 | ^ 3 Exclusive "轺 ,,,,,,", i · ~! Igg钱 jigi | Continue hall Ai noodle ill 有用以設定熱水供應的目標溫度之溫度設定部,且前 述負荷設定部係以前述溫度設定部之設定值為基準算 出加熱量。 5 10 15 1心如申請專利範圍第17項之熱泵式熱水供應裝置,更具 有用以檢測前述熱水供應迴路的流出熱水溫度之熱水 溫度檢測部,且前述負荷設定部係以前述流出熱水溫 度與目標溫度之偏差為基準算出第1加熱量。 19. 如申請專利範圍第18項之熱泵式熱水供應裝置,更具 有用以檢測前述給水管的給水溫度之水溫檢測部及用 以檢測熱水供應迴路的流量之流量檢測部,且以前述 水溫檢測部與前述溫度設定部與前述流量檢測部之值 為基準算出第2加熱量,並將前述第1加熱量與第2 加熱量相加。 20. 如申請專利範圍第14項之熱泵式熱水供應裝置,其中 前述負荷設定部係具有用以訂定滿足前述熱泵循環機 構與前述熱交換器之至少一者的熱反應延遲之熱量之 升高設定部, 且於設定加熱量時加入前述升高設定部之設定值 20 21.如申請專利範圍第14項之熱泵式熱水供應裝置,其中 前述加熱控制部可控制前述壓縮機之轉數。 22. 如申請專利範圍第14項之熱泵式熱水供應裝置,其中 前述加熱控制部係用以控制前述冷媒流路之阻力。 23. 如申請專利範圍第22項之熱泵式熱水供應裝置,更具 47 574491 :申請專利範圍 有用以檢測前述給水管的給水溫度之水溫檢測部, 且刖述冷媒流路之阻力控制係依照前述水溫檢測 部之檢測溫度來進行。 5 24·如申請專利範圍第14項之熱泵式熱水供應裝置,其中 前述加熱控制部可控制前述吸熱器之吸熱量。 25·如申請專利範圍第14項之熱泵式熱水供應裝置,其中 前述加熱控制部可變更前述熱交換器中之前述水流路 内的流速與流量之至少一者。 10 26·如申請專利範圍第14項之熱泵式熱水供應裝置,更具 有用以檢測氣溫之氣溫檢測部, 且前述加熱控制部係依照前述氣溫檢測部之檢測 值來控制前述熱交換器之加熱量。 27· —種熱泵式熱水供應裝置,包含有: 15 Γα 熱栗循環機構,具有:多數壓縮機、放熱器、減 壓部、吸熱器及使前述壓縮機、前述放熱器、前述減 壓部及前述吸熱器構成為閉路之冷媒流路; 熱交換器’具有用以與前述冷媒流路進行熱交換 之水流路; 給水管’用以將自來水供給至前述水流路;及 熱水供應迴路,係連接成可從前述水流路通水至 熱水供應末端。 28· —種熱泵式熱水供應裝置,包含有: 多數熱泵循環機構,具有··壓縮機、放熱器、減 壓部、吸熱器及使前述壓縮機、前述放熱器、前述減 48 574491 、 、、、'、:、、 、、、 、、、、、、'、、 :' 、 、、” 、、、、、、 、、、、 s' % $、、、、、、、 、、、、 、 、、、:ί i *>、、、、、、、、'、·、、、、、 χ, 、'”、、、、·'、 、、S -¾ N sis S 、 、、s、、、、、、 、、、、'、'、、、::、、'、%'、、、·、、 、'、:; ''0、、、 、'、 、、5'、vl·、、、、、Ϊ、、、、''、、、、'_、' ϊ Ί'、、 、' i > v、、、、i、、i、' ' \ '、'、、 、、 、、 、、 、,、' Ϊ '、''、、、 、 ή、ζ、、、入 ' '、 、 、'、 、 、 壓部及前述吸熱器構成為閉路之冷媒流路; 熱交換器,具有用以與前述冷媒流路進行熱交換 之水流路; 5 給水管,係用以將自來水供給至前述水流路;及 熱水供應迴路,係連接成從前述水流路至熱水供 應末端可通水者。 29. 如申請專利範圍第28項之熱泵式熱水供應裝置,係將 前述熱交換器與前述多數熱泵循環機構分割為複數個 單元而配置。 10 30. 如申請專利範圍第28項之熱泵式熱水供應裝置,係依 照熱水供應負荷來變更前述多數熱泵循環機構之運轉 台數量。 15 31. 如申請專利範圍第1、14、27或28項中任一項之熱泵 式熱水供應裝置,其中前述熱泵循環機構為冷媒壓力 在臨界壓力以上之超臨界熱泵循環機構,且藉由升壓 至臨界壓力以上之該冷媒來加熱前述熱交換器中之前 述水流路的流水。 32. 如申請專利範圍第1、14、27或28項中任一項之熱泵 式熱水供應裝置,係於前述熱交換器中,使前述冷媒 流路之流動方向與前述水流路之流動方向相對。 49 20There is a temperature setting section for setting the target temperature of the hot water supply, and the load setting section calculates the heating amount based on the setting value of the temperature setting section. 5 10 15 1 The heat pump type hot water supply device according to item 17 of the patent application scope further includes a hot water temperature detection section for detecting the temperature of the hot water flowing out of the hot water supply circuit, and the load setting section is based on the aforementioned The difference between the outflow hot water temperature and the target temperature is used as a reference to calculate the first heating amount. 19. For example, the heat pump hot water supply device of the scope of application for patent No. 18 further includes a water temperature detection section for detecting the water supply temperature of the water supply pipe and a flow detection section for detecting the flow of the hot water supply circuit. The second heating amount is calculated based on the values of the water temperature detection section, the temperature setting section, and the flow detection section, and the first heating amount and the second heating amount are added. 20. The heat pump-type hot water supply device according to item 14 of the scope of patent application, wherein the load setting section has a heat increase for setting a heat quantity that satisfies a thermal reaction delay of at least one of the heat pump circulation mechanism and the heat exchanger. High setting part, and add the set value of the aforementioned rising setting part 20 when setting the heating amount. 21. For example, the heat pump type hot water supply device of the scope of application for patent No. 14, wherein the heating control part can control the rotation speed of the compressor. . 22. The heat pump hot water supply device according to item 14 of the application, wherein the heating control unit is used to control the resistance of the refrigerant flow path. 23. For example, the heat pump type hot water supply device of item 22 of the scope of patent application, 47 574491: The scope of the patent application is a water temperature detection unit for detecting the water supply temperature of the water supply pipe, and the resistance control system of the refrigerant flow path is described. This is performed in accordance with the detection temperature of the water temperature detection section. 5 24. The heat pump hot water supply device according to item 14 of the scope of patent application, wherein the heating control unit can control the heat absorption of the heat sink. 25. The heat pump hot water supply device according to item 14 of the patent application scope, wherein the heating control unit may change at least one of a flow velocity and a flow rate in the water flow path in the heat exchanger. 10 26 · The heat pump hot water supply device according to item 14 of the scope of patent application, further includes an air temperature detecting section for detecting the air temperature, and the heating control section controls the heat exchanger according to the detection value of the air temperature detecting section. Amount of heating. 27 · —A heat pump type hot water supply device, including: 15 Γα heat pump circulation mechanism, including: most compressors, radiators, decompression units, heat sinks, and compressors, radiators, and decompression units And the aforementioned heat sink is configured as a closed refrigerant flow path; the heat exchanger 'has a water flow path for heat exchange with the aforementioned refrigerant flow path; a water supply pipe' is used to supply tap water to the aforementioned water flow path; and a hot water supply circuit, It is connected so that water can flow from the water flow path to the hot water supply end. 28. A heat pump type hot water supply device, including: most heat pump circulation mechanisms, including a compressor, a radiator, a decompression unit, a heat absorber, and the compressor, the radiator, the aforementioned minus 48 574491, ,,,,,,,,,,, ,,,,,,,,, ::,, ,,,,,,,,,,,,,, s'% $ ,,,,,,,,,,,, ,,,,,: ί i * > ,,,,,,,,,,,,,,,,, χ,, "" ,,,, ',,,, S -¾ N sis S, ,, s ,,,,,,,,,,,,,,,,,, :: ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, · ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,-,,,,,,,,, and i ,,,,,,,, 'Ϊ', '',,,, price, ζ, ,, '',,,, ',,,, and the heat sink constitute the closed-circuit refrigerant flow path; heat exchange A water flow path for heat exchange with the refrigerant flow path; 5 a water supply pipe, In the water supplied to the water flow path; and a hot water supply circuit, connected to the system's water supply tip may pass from the water passage to the hot water. 29. For example, the heat pump hot water supply device according to item 28 of the scope of patent application, the heat exchanger and the majority of the heat pump circulation mechanisms are divided into a plurality of units and arranged. 10 30. For the heat pump type hot water supply device under the scope of patent application No. 28, the number of operating tables of most of the aforementioned heat pump circulation mechanisms is changed according to the hot water supply load. 15 31. The heat pump type hot water supply device according to any one of the claims 1, 14, 27, or 28, wherein the heat pump circulation mechanism is a supercritical heat pump circulation mechanism with a refrigerant pressure above a critical pressure, and by The refrigerant that has been raised above the critical pressure heats the flowing water in the water flow path in the heat exchanger. 32. If the heat pump type hot water supply device according to any one of the scope of application for patents 1, 14, 27 or 28 is in the heat exchanger, the flow direction of the refrigerant flow path and the flow direction of the water flow path relatively. 49 20
TW92102791A 2002-02-12 2003-02-11 Heat pump hot water supply device TW574491B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2002033648A JP3743375B2 (en) 2002-02-12 2002-02-12 Heat pump water heater
JP2002033650A JP3815341B2 (en) 2002-02-12 2002-02-12 Heat pump water heater
JP2002041048A JP3778102B2 (en) 2002-02-19 2002-02-19 Heat pump water heater

Publications (2)

Publication Number Publication Date
TW200303407A TW200303407A (en) 2003-09-01
TW574491B true TW574491B (en) 2004-02-01

Family

ID=27738902

Family Applications (1)

Application Number Title Priority Date Filing Date
TW92102791A TW574491B (en) 2002-02-12 2003-02-11 Heat pump hot water supply device

Country Status (7)

Country Link
US (1) US7316267B2 (en)
EP (1) EP1475576A4 (en)
KR (2) KR100567491B1 (en)
CN (1) CN100535542C (en)
HK (1) HK1065841A1 (en)
TW (1) TW574491B (en)
WO (1) WO2003069236A1 (en)

Families Citing this family (76)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3742356B2 (en) * 2002-03-20 2006-02-01 株式会社日立製作所 Heat pump water heater
US6968708B2 (en) * 2003-06-23 2005-11-29 Carrier Corporation Refrigeration system having variable speed fan
JP2006162101A (en) * 2004-12-03 2006-06-22 Hitachi Home & Life Solutions Inc Heat pump water heater
EP1853856A1 (en) 2005-02-18 2007-11-14 Carrier Corporation Co2-refrigeration device with heat reclaim
JP4284290B2 (en) * 2005-03-24 2009-06-24 日立アプライアンス株式会社 Heat pump water heater
US7543456B2 (en) 2006-06-30 2009-06-09 Airgenerate Llc Heat pump liquid heater
US20090159259A1 (en) * 2006-06-30 2009-06-25 Sunil Kumar Sinha Modular heat pump liquid heater system
JP4245044B2 (en) * 2006-12-12 2009-03-25 ダイキン工業株式会社 Refrigeration equipment
US7708010B2 (en) * 2007-03-05 2010-05-04 Taco Inc. Solar heating systems
RU2426957C1 (en) * 2007-06-12 2011-08-20 Данфосс А/С Procedure for control of vapour-compressor system
KR100866738B1 (en) * 2007-07-30 2008-11-03 주식회사 귀뚜라미 범양냉방 Hybrid heat pump type heat and cooling system with feeding steam water
CN101240962B (en) * 2008-01-18 2010-06-02 西安交通大学 Carbon dioxide heat pump control method based on pressure-temperature
JP5216368B2 (en) * 2008-02-29 2013-06-19 日立アプライアンス株式会社 Heat pump water heater
DE102008016663A1 (en) * 2008-04-01 2009-10-08 Efficient Energy Gmbh Condenser for a heat pump and heat pump
KR100985384B1 (en) * 2008-06-27 2010-10-05 주식회사 경동네트웍 Method for controlling a hot water temperature in using low flux in hot water supply system
DE102008049954A1 (en) * 2008-10-02 2010-04-08 Thomas Hahn Device for the use and storage of solar and environmental heat, usable all year round efficiently
JP5042262B2 (en) * 2009-03-31 2012-10-03 三菱電機株式会社 Air conditioning and hot water supply complex system
CN102369397B (en) * 2009-04-13 2014-03-26 松下电器产业株式会社 Heat pump type heating device
WO2010137120A1 (en) * 2009-05-26 2010-12-02 三菱電機株式会社 Heat pump type hot water supply device
US8385729B2 (en) 2009-09-08 2013-02-26 Rheem Manufacturing Company Heat pump water heater and associated control system
KR100947309B1 (en) * 2009-09-10 2010-03-16 에이치에스지(주) Heat pump for supplying cool and hot water
KR101321549B1 (en) * 2009-11-20 2013-10-30 엘지전자 주식회사 Heat pump
KR101179812B1 (en) * 2009-12-03 2012-09-04 주식회사 경동나비엔 Pipe connecting structure of water heater
FR2955381A1 (en) 2010-01-19 2011-07-22 Michel Charles Albert Barbizet METHOD FOR THE VALORISATION OF LOW TEMPERATURE THERMAL ENERGY IN MULTI-GENERATION SYSTEMS
EP2530406B1 (en) * 2010-01-29 2017-03-22 Daikin Industries, Ltd. Heat pump system
KR20110097203A (en) * 2010-02-25 2011-08-31 삼성전자주식회사 Heat pump system and control method thereof
US9562696B2 (en) 2010-04-15 2017-02-07 Mitsubishi Electric Corporation Hot water supply system control apparatus and hot water supply system control program and hot water supply system operating method
JP5705455B2 (en) * 2010-04-28 2015-04-22 三菱重工業株式会社 Heat pump water heater using CO2 refrigerant
CN101957069A (en) * 2010-04-30 2011-01-26 冼泰来 Transcritical carbon dioxide solar water heater
CN102313358A (en) * 2010-07-01 2012-01-11 珠海格力节能环保制冷技术研究中心有限公司 Control method for exhaust pressure of carbon-dioxide heat-pump water heater
EP2413044B1 (en) * 2010-07-30 2015-10-28 Grundfos Management A/S Domestic water heating unit
US20100300377A1 (en) * 2010-08-11 2010-12-02 Buescher Thomas P Water heater apparatus with differential control
US9182159B2 (en) * 2010-10-14 2015-11-10 Purpose Company Limited Water heater and control method therefor
KR101212698B1 (en) 2010-11-01 2013-03-13 엘지전자 주식회사 Heat pump type speed heating apparatus
KR101203579B1 (en) * 2010-11-05 2012-11-21 엘지전자 주식회사 Speed heating apparatus with air conditioner and Control process of the same
JP5758913B2 (en) * 2010-12-24 2015-08-05 株式会社前川製作所 Operation control method of heat pump device
KR101212683B1 (en) * 2010-12-30 2013-01-09 엘지전자 주식회사 Hot water supply device associated with heat pump
JP6076583B2 (en) * 2011-01-19 2017-02-08 三菱重工業株式会社 heat pump
DE102011083393A1 (en) * 2011-09-26 2013-03-28 Siemens Aktiengesellschaft Heat pump with heat pump and method for operating a heat pump with heat pump
JP5452581B2 (en) * 2011-12-29 2014-03-26 三菱電機株式会社 HEAT PUMP SYSTEM AND HEAT PUMP DEVICE CONTROL METHOD
JP5494696B2 (en) * 2012-02-27 2014-05-21 ダイキン工業株式会社 Heat pump equipment energy management device
US9244466B2 (en) * 2012-07-24 2016-01-26 General Electric Company Electronic mixing valve in standard hot water heater
CA2880183A1 (en) * 2012-07-30 2014-02-20 Efficaxenergy Ab System, module and valve for domestic hot water heaters
CN102999054A (en) * 2012-11-29 2013-03-27 成都硅宝科技股份有限公司 Continuous and automatic liquid metering and feeding system and method for sealant production
CN103776162A (en) * 2012-12-26 2014-05-07 苟仲武 Heat pump concurrent heating temperature rise type efficient heat exchanger and method for conducting heat exchange through heat pump concurrent heating temperature rise type efficient heat exchanger
JP6048158B2 (en) * 2013-01-18 2016-12-21 株式会社ノーリツ Water heater
JP2014153044A (en) * 2013-02-14 2014-08-25 Panasonic Corp Hot water storage type hot water supply machine
US9267696B2 (en) * 2013-03-04 2016-02-23 Carrier Corporation Integrated membrane dehumidification system
US9389000B2 (en) * 2013-03-13 2016-07-12 Rheem Manufacturing Company Apparatus and methods for pre-heating water with air conditioning unit or heat pump
US9464840B2 (en) * 2013-06-05 2016-10-11 Hill Phoenix, Inc. Gas defrosting system for refrigeration units using fluid cooled condensers
FR3008172A1 (en) * 2013-07-03 2015-01-09 Jean Francois Sailhan COLD PRODUCTION FACILITY COMPRISING IMPROVED CONDENSATION MEANS AND METHOD FOR IMPLEMENTING THE SAME
DE102013214063A1 (en) * 2013-07-16 2015-01-22 Robert Bosch Gmbh Method for controlling a compressor of a heat pump
EP2829819B1 (en) * 2013-07-25 2016-03-02 IMAT S.p.A. Heat-pump water heater for domestic purposes
FR3009612B1 (en) * 2013-08-09 2018-12-07 Zodiac Pool Care Europe SYSTEM AND METHOD FOR CONTROLLING HEAT PUMP FOR SWIMMING POOL
DE102013015368A1 (en) * 2013-09-11 2015-03-12 Hydac Cooling Gmbh tempering
EP2860469A1 (en) * 2013-10-11 2015-04-15 Nederlandse Organisatie voor toegepast -natuurwetenschappelijk onderzoek TNO Water heater
FR3018902A1 (en) * 2014-03-19 2015-09-25 Electricite De France HOT WATER PRODUCTION FACILITY AND METHOD FOR CONTROLLING THIS INSTALLATION
US9945587B2 (en) 2014-09-02 2018-04-17 Rheem Manufacturing Company Apparatus and method for hybrid water heating and air cooling and control thereof
US9696043B2 (en) * 2015-03-09 2017-07-04 Haier Us Appliance Solutions, Inc. Hot water heater systems and methods for controlling electronic mixing valves
US20160320074A1 (en) * 2015-04-30 2016-11-03 King Fahd University Of Petroleum And Minerals Fluid supply system with temperature control for fluid conservation
CN105605773A (en) * 2016-01-25 2016-05-25 中山昊天节能科技有限公司 Integral type air-energy water boiler
CN105953425A (en) * 2016-06-15 2016-09-21 许鸣华 Direct bathing type air energy water heater
JP2018013257A (en) * 2016-07-19 2018-01-25 パナソニックIpマネジメント株式会社 Heat Pump Water Heater
US10323859B2 (en) 2016-10-27 2019-06-18 King Fahd University Of Petroleum And Minerals Water mixing system for thermoregulating water
CN106765943B (en) * 2016-12-16 2019-08-16 广东美的暖通设备有限公司 Control method, control device and the constant speed Air-Cooled Heat Pump Unit of outer machine blower
IT201800006559A1 (en) * 2018-06-21 2019-12-21 IMPROVED INSTALLATION FOR INSTANTANEOUS PRODUCTION OF HOT WATER FOR SANITARY USE
CN109405347B (en) * 2018-12-05 2021-08-06 江苏天舒电器有限公司 Control method of multi-stage heat utilization heat pump control system for bathroom
CN113785162B (en) * 2019-05-10 2023-02-17 三菱电机株式会社 Heat storage system
WO2021051185A1 (en) * 2019-09-20 2021-03-25 Camus Hydronics Ltd. System and method for controlling water heater output temperature
CN110726245B (en) * 2019-10-08 2021-05-25 广东纽恩泰新能源科技发展有限公司 Household variable-frequency direct-heating air energy heat pump water heater
KR20210111546A (en) * 2020-03-03 2021-09-13 코웨이 주식회사 Humidification Module with Humidification Control Function and Multi-Functional Storage System Having Same
CN111609560B (en) * 2020-04-20 2022-05-31 芜湖美的厨卫电器制造有限公司 Control method of gas water heater, gas water heater and computer readable storage medium
US20220357053A1 (en) * 2021-05-10 2022-11-10 Richard Curtis Bourne Heat pump human washing appliance
FR3125867B1 (en) * 2021-07-27 2023-11-24 Soc Ind De Chauffage Sic Thermodynamic storage and heating system with optimized control
DE102022200651A1 (en) 2022-01-20 2023-07-20 Robert Bosch Gesellschaft mit beschränkter Haftung Method for operating the heat pump system; Heat pump system for such a method
WO2024094865A1 (en) * 2022-11-03 2024-05-10 Gea Process Engineering A/S Method and system for controlling a heat pump

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2575325A (en) * 1948-02-14 1951-11-20 American Gas And Electric Comp Heat pump system
JPS5658067A (en) 1979-10-15 1981-05-20 Teijin Ltd Production of artificial leather
JPS58102052A (en) 1981-12-14 1983-06-17 Hitachi Ltd Heat pump type water heating equipment
DE3308447C2 (en) * 1983-03-10 1991-07-18 Wilhelm 2849 Goldenstedt Hakemann Device for generating hot water
JPS6053733A (en) * 1983-09-05 1985-03-27 Matsushita Electric Ind Co Ltd Heat pump hot-water supplying machine
JPS6117849A (en) 1984-07-03 1986-01-25 Matsushita Electric Ind Co Ltd Heat pump type water heating and hot-water supplying device
JPS61246541A (en) * 1985-04-22 1986-11-01 Yoshitomi Shiba Heat pump type hot water supplier
US4680941A (en) * 1986-05-21 1987-07-21 Richardson Elvet M Waste heating recovery system
JPH02223767A (en) 1989-02-23 1990-09-06 Fujitsu General Ltd Heat pump type hot water supply equipment
US5050394A (en) * 1990-09-20 1991-09-24 Electric Power Research Institute, Inc. Controllable variable speed heat pump for combined water heating and space cooling
JP3371622B2 (en) 1995-06-16 2003-01-27 三菱電機株式会社 Heat pump hot water supply equipment
JPH10253155A (en) * 1997-03-14 1998-09-25 Tokyo Electric Power Co Inc:The Heat exchanger unit
JP3800721B2 (en) * 1997-05-14 2006-07-26 松下電器産業株式会社 Heat pump type water heater
JP3663828B2 (en) 1997-05-21 2005-06-22 松下電器産業株式会社 Heat pump bath water supply system
JP3227651B2 (en) * 1998-11-18 2001-11-12 株式会社デンソー Water heater
JP3642233B2 (en) * 1999-08-03 2005-04-27 松下電器産業株式会社 Water heater
JP4104805B2 (en) 2000-03-30 2008-06-18 三菱電機株式会社 Heat pump water heater
JP2001304701A (en) * 2000-04-19 2001-10-31 Denso Corp Heat pump type water heater
JP4465903B2 (en) * 2000-04-28 2010-05-26 株式会社デンソー Air conditioner for vehicles
JP3738672B2 (en) * 2000-06-20 2006-01-25 株式会社デンソー Heat pump water heater
JP4059616B2 (en) * 2000-06-28 2008-03-12 株式会社デンソー Heat pump water heater
JP3801006B2 (en) * 2001-06-11 2006-07-26 ダイキン工業株式会社 Refrigerant circuit
US7076964B2 (en) * 2001-10-03 2006-07-18 Denso Corporation Super-critical refrigerant cycle system and water heater using the same
JP4311115B2 (en) * 2002-09-17 2009-08-12 株式会社デンソー Air conditioner

Also Published As

Publication number Publication date
US7316267B2 (en) 2008-01-08
KR100567488B1 (en) 2006-04-03
WO2003069236A1 (en) 2003-08-21
HK1065841A1 (en) 2005-03-04
CN100535542C (en) 2009-09-02
EP1475576A4 (en) 2009-12-09
KR20040000484A (en) 2004-01-03
CN1509396A (en) 2004-06-30
EP1475576A1 (en) 2004-11-10
TW200303407A (en) 2003-09-01
US20040144528A1 (en) 2004-07-29
KR100567491B1 (en) 2006-04-03
KR20050105521A (en) 2005-11-04

Similar Documents

Publication Publication Date Title
TW574491B (en) Heat pump hot water supply device
US9010281B2 (en) Hot water supply system
JP4124258B2 (en) Heat pump water heater
JP4971838B2 (en) Water heater and hot water heater
JP4912928B2 (en) Heat pump hot water storage / heating system
JP2009281650A (en) Heating system
JP3925433B2 (en) Heat pump water heater
JP2006200888A (en) Heat pump hot water supply apparatus
JP5542617B2 (en) Heating system
JP2004218908A (en) Water heater
JP3778102B2 (en) Heat pump water heater
JP4290115B2 (en) Hot water storage hot water heater
JP6014435B2 (en) Three-fluid heat exchanger
JP2009281644A (en) Heating system
JP2004218909A (en) Water heater
JP5667856B2 (en) Water heater
JP3743375B2 (en) Heat pump water heater
JP2008151450A (en) Heat storage type hot water supply apparatus
JP3945361B2 (en) Heat pump water heater
JP2009008386A (en) Hot water storage type hot water supply heating system
JP4424265B2 (en) Hot water storage water heater
JP4515883B2 (en) Hot water storage water heater
JP2008045826A (en) Hot-water storage type hot water supply heater
JP2004156845A (en) Heat pump water heater device
JP2004232912A (en) Heat pump water heater

Legal Events

Date Code Title Description
GD4A Issue of patent certificate for granted invention patent
MM4A Annulment or lapse of patent due to non-payment of fees